US5061745A - Flame-retardant, high-impact polycarbonate molding compounds - Google Patents

Flame-retardant, high-impact polycarbonate molding compounds Download PDF

Info

Publication number
US5061745A
US5061745A US07/355,957 US35595789A US5061745A US 5061745 A US5061745 A US 5061745A US 35595789 A US35595789 A US 35595789A US 5061745 A US5061745 A US 5061745A
Authority
US
United States
Prior art keywords
weight
parts
styrene
halogen
molding compounds
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US07/355,957
Inventor
Dieter Wittmann
Horst Peters
Jochen Schoeps
Hans-Jurgen Kress
Josef Buekers
Karl-Heinz Ott
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Bayer AG
Original Assignee
Bayer AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=6355881&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=US5061745(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Bayer AG filed Critical Bayer AG
Assigned to BAYER AKTIENGESELLSCHAFT, A CORP. OF GERMANY reassignment BAYER AKTIENGESELLSCHAFT, A CORP. OF GERMANY ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: BUEKERS, JOSEF, KRESS, HANS-JURGEN, OTT, KARL-HEINZ, PETERS, HORST, SCHOEPS, JOCHEN, WITTMANN, DIETER
Application granted granted Critical
Publication of US5061745A publication Critical patent/US5061745A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/49Phosphorus-containing compounds
    • C08K5/51Phosphorus bound to oxygen
    • C08K5/52Phosphorus bound to oxygen only
    • C08K5/521Esters of phosphoric acids, e.g. of H3PO4
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/49Phosphorus-containing compounds
    • C08K5/51Phosphorus bound to oxygen
    • C08K5/53Phosphorus bound to oxygen bound to oxygen and to carbon only
    • C08K5/5317Phosphonic compounds, e.g. R—P(:O)(OR')2
    • C08K5/5333Esters of phosphonic acids
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L69/00Compositions of polycarbonates; Compositions of derivatives of polycarbonates

Definitions

  • This invention relates to high-impact, flame-retardant, thermoplastic polycarbonate molding compounds consisting of
  • thermoplastic, halogen-free, aromatic polycarbonates based on diphenols corresponding to formula (II),
  • B.2 95 to 10 parts by weight, preferably 70 to 20 parts by weight, based on B), of a rubber having a glass temperature T G of ⁇ 10° C.
  • component E) 0.05 to 5 parts by weight, preferably 0.1 to 1 part by weight and, more preferably, 0.1 to 0.5 part by weight, based on 100 parts by weight of A)+B)+optionally C), of a tetrafluoroethylene polymer having average particle sizes of from 0.05 to 1000 ⁇ m, a density of 1.2 to 2.3 g/cm 3 and a fluorine content of 65 to 76% by weight, component E) preferably being used in the form of a coagulated mixture of emulsions of the tetrafluoroethylene polymers E) having an average particle size of 0.05 to 20 ⁇ and a density of 1.2 to 1.9 g/cm 3 with emulsions of graft polymers B) and the ratio by weight of graft polymer B) to the tetrafluoroethylene polymer E) being from 95:5 to 60:40 and the content of addition quantities B), based on 100 parts by weight A)+B) and optionally C), being from 0.1 to
  • DE-OS 3 322 260 (Le A 22 391) describes flame-retardant thermoplastic molding compounds of
  • thermoplastic polymer 0 to 50 parts by weight of a thermoplastic polymer
  • DE-OS 3 430 234 (Le A 22 925) describes flame-resistant thermoplastic polymer mixtures containing special, halogen-free polycarbonates of 50 mol % to 100 mol % tetraalkylated bisphenol carbonate structural units, halogen-free styrene polymers and/or halogen-free graft polymers, halogen-free phosphate esters and, optionally, tetrafluoroethylene polymers.
  • EP-OS 0 174 493 (Le A 23 043-EP) describes thermoplastic molding compounds consisting of
  • thermoplastic aromatic polycarbonate A) 20 to 85 parts by weight of a thermoplastic aromatic polycarbonate
  • DE-OS 3 521 388 (Le A 23 877) describes thermoplastic flame-resistant molding compounds containing halogen-free polycarbonates, copolymers of styrenes with maleic anhydride, phosph(on)ate esters, tetrafluoroethylene polymers and 0.1 to 3 parts by weight graft polymers, the graft polymers again having been co-precipitated with the tetrafluoroethylene polymers.
  • these molding compounds achieve a V-O rating for a thickness of 1.6 mm, their toughness, flow line strength and resistance to stress crazing are inadequate for numerous applications.
  • DE-OS 3 523 314 (Le A 23 940) describes high-impact, flame-retardant molding compounds of halogen-free polycarbonates, halogen-free styrene-acrylonitrile copolymers, phosphorus compounds, tetrafluoroethylene polymers and 0.1 to 3 parts by weight graft polymers, the graft polymers again having been co-precipitated with the tetrafluoroethylene polymers.
  • the toughness, flow line strength and resistance to stress crazing of the molding compounds according to DE-OS 3 523 314 is inadequate for certain applications, particularly in the case of complicated, flame-proofed moldings, such as housing components, where design-related openings, webs and the like call for as high a level of the above-mentioned properties as possible.
  • thermoplastic, halogen-free aromatic polycarbonate A) 40 to 95 parts by weight, based on 100 parts by weight A)+B)+C), of a thermoplastic, halogen-free aromatic polycarbonate,
  • F stabilizers, pigments, flow aids, mold release agents and/or antistatic agents.
  • molding compounds of the type in question have the disadvantage of a narrower processing scope and lower flow line strength than the molding compounds according to the invention.
  • DE-OS 3 628 904 (Le A 24 683) describes high-impact flame-retardant polycarbonate molding compounds consisting of
  • DE-OS 3 629 546 (Le-A 24 695) describes high-impact flame-retardant molding compounds containing
  • component D) being used in the form of a coagulated mixture of emulsions of the tetrafluoroethylene polymers D) with emulsions of at most 3 parts by weight, but at least 0.1 part by weight, based on 100 parts by weight of the sum of components A) and B), of graft polymers
  • the technical advantage of the molding compounds according to the invention lies in the extremely advantageous combination of toughness, resistance to stress crazing and flame resistance, the latter being achieved without any halogen (Br, Cl) and metal compounds.
  • Thermoplastic, halogen-free, aromatic polycarbonates of component A) suitable for use in accordance with the invention are those based on diphenols corresponding to formula (II) ##STR6## in which A is a single bond, C 1 -C 5 alkylene, C 2 -C 5 alkylidene, C 5 -C 6 cycloalkylidene, --S-- or --SO 2 --.
  • Suitable diphenols corresponding to formula (II) are, for example, hydroquinone, resorcinol, 4,4'-dihydroxydiphenyl, 2,2-bis-(4-hydroxyphenyl)-propane, 2,4-bis-(4-hydroxyphenyl)-2-methyl butane or 1,1-bis-(4-hydroxyphenyl)cyclohexane.
  • Preferred diphenols corresponding to formula (II) are 2,2-bis-(4-hydroxyphenyl)-propane and 1,1-bis-(4-hydroxyphenyl)-cyclohexane.
  • diphenols corresponding to formula (II) are either known from the literature or may be produced by methods known from the literature.
  • polycarbonates of component A) suitable for use in accordance with the invention is known from the literature and may be carried out, for example, with phosgene by the interfacial process or with phosgene by the homogeneous-phase process (so-called pyridine process), the particular molecular weight to be established being obtained in known manner through a corresponding quantity of known chain terminators.
  • Suitable chain terminators are, for example, monophenols, such as phenol itself, p-cresol, p-tert.-butylphenol and p-isooctylphenol.
  • the polycarbonates of component A) suitable for use in accordance with the invention have average molecular weights (M w , as measured for example by ultracentrifugation or by scattered light measurement) of from 10,000 to 200,000 and preferably from 20,000 to 80,000.
  • polycarbonates of component A) suitable for use in accordance with the invention are both homopolycarbonates and also copolycarbonates.
  • polycarbonates of component A) suitable for use in accordance with the invention may be branched in known manner, preferably through the incorporation of 0.05 to 2.0 mol %, based on the sum of the diphenols used, of trifunctional or more than trifunctional compounds, for example those containing three or more than three phenolic OH groups.
  • halogen-free polycarbonates are understood to be polycarbonates of halogen-free diphenols, halogen-free chain terminators and, optionally, halogen-free branching agents, the content of small quantities (ppm) of hydrolyzable chlorine, resulting for example from the production of the polycarbonates with phosgene by the interfacial process, not counting as "halogen-containing" in the context of the invention.
  • Polycarbonates such as these having ppm contents of hydrolyzable chlorine are halogen-free polycarbonates in the context of the invention.
  • Rubbers suitable for the production of the halogen-free graft polymers B) are, in particular, polybutadiene, butadiene/styrene copolymers (both also copolymerized with up to 30% by weight, based on the weight of the rubber, of a lower alkyl ester of acrylic or methacrylic acid, such as methyl methacrylate, ethyl acrylate, methyl acrylate or ethyl methacrylate), polyisoprene, alkyl acrylate rubbers (of C 1 -C 8 alkyl acrylates, particularly ethyl, butyl, ethyl hexyl acrylate).
  • the alkyl acrylate rubbers may optionally contain up to 30% by weight, based on the weight of the rubber, of such monomers as vinyl acetate, acrylonitrile, styrene, methyl methacrylate and/or vinyl ethers in copolymerized form and also relatively small quantities, preferably up to 5% by weight, based on the weight of the rubber, of crosslinking, ethylenically unsaturated monomers.
  • Crosslinking agents such as these are, for example, alkylenediol di-(meth)-acrylates, polyester di-(meth)-acrylates, divinylbenzene, trivinylbenzene, triallyl cyanurate, allyl (meth)acrylate, butadiene or isoprene.
  • Suitable acrylate rubbers are those which contain a crosslinked diene rubber of one or more conjugated dienes and, optionally, an ethylenically unsaturated monomer, such as styrene and/or acrylonitrile, as core.
  • Other suitable rubbers are, for example, EPDM rubbers, i.e. rubbers of ethylene, propylene and an unconjugated diene, and also silicone rubbers.
  • Preferred rubbers for the production of the graft polymers B) are diene and alkyl acrylate rubbers.
  • the rubbers are present in the graft polymers B) in the form of at least partly crosslinked particles having an average particle size from 0.09 to 5 ⁇ m and more especially from 0.1 to 1 ⁇ m.
  • the graft polymers B) are produced by radical graft copolymerization of the monomer mixtures defind at the beginning of B.1.1) and B.1.2) in the presence of the rubbers B.2) to be grafted and are all known.
  • Preferred production processes for the graft polymers B) are emulsion, solution, bulk or suspension polymerization.
  • Particularly preferred graft polymers B) are the so-called ABS polymers.
  • Nucleus-substituted styrenes are understood to be nucleus-alkylated styrenes, such as for example p-methyl styrene.
  • Copolymers of component C) are often formed as secondary products in the graft polymerization for the production of component B), particularly when large quantities of monomers are grafted onto small quantities of rubber.
  • the quantity of copolymer C) to be used in accordance with the invention does not include these secondary graft polymerization products.
  • copolymers of component C) are resin-like, thermoplastic and rubber-free.
  • Particularly preferred copolymers C) are those of styrene with acrylonitrile and, optionally, with methyl methacrylate, of ⁇ -methyl styrene with acrylonitrile and, optionally, with methyl methacrylate or of styrene and ⁇ -methyl styrene with acrylonitrile and, optionally, with methyl methacrylate.
  • thermoplastic copolymer C Particularly preferred ratios by weight in the thermoplastic copolymer C) are 60 to 80% by weight C.1) and 40 to 20% by weight C.2).
  • the styrene-acrylonitrile copolymers of component C) are known and may be produced by radical polymerization, more especially by emulsion, suspension, solution or bulk polymerization.
  • the copolymers of component C) preferably have molecular weights M (weight average, as determined by light scattering or sedimentation) of from 15,000 to 200,000.
  • halogen-free phosphorus compounds of component D) suitable for use in accordance with the invention are generally known (cf. for example Ullmann, Enzyklopadie der ischen Chemie, Vol. 18, pages 301 et seq., 1979; Houben-Weyl, Methoden der Organischen Chemie, Vol. 12/1, page 43; Beilstein, Vol. 6, page 177).
  • Phosphorus compounds of component D), formula (I), suitable for use in accordance with the invention are, for example, triphenylphosphate, tricresylphosphate, diphenyl-2-ethyl cresylphosphate, tri-(isopropylphenyl)-phosphate, methylphosphonic acid diphenyl ester, phenyl phosphonic acid diethyl ester, diphenyl cresylphosphate and tributylphosphate.
  • the tetrafluoroethylene polymers of component e) suitable for use in accordance with the invention are polymers having fluorine contents of from 65 to 76% by weight and preferably from 70 to 76% by weight.
  • Examples of such polymers are polytetrafluoroethylene, tetrafluoroethylene-hexafluoropropylene copolymers or tetrafluoroethylene copolymers containing small quantities of fluorine-free, copolymerizable, ethylenically unsaturated monomers.
  • the polymers are known and may be produced by known methods, for example by polymerization of tetrafluoroethylene in aqueous medium with a catalyst forming free radicals, for example sodium, potassium or ammonium peroxydisulfate, under pressures of 7 to 71 kg/cm 2 and at temperatures of from 0° to 200° C. and preferably at temperatures of 20° to 100° C. (For further particulars, cf. for example U.S. Pat. No. 2,393,967.) Depending on the form in which they are used, these materials may have a density of 1.2 to 2.3 g/cm 3 and an average particle size of 0.05 to 1000 ⁇ m.
  • a catalyst forming free radicals for example sodium, potassium or ammonium peroxydisulfate
  • preferred polytetrafluoroethylenes have average particle sizes from 0.05 to 20 ⁇ m and preferably from 0.08 to 10 ⁇ m and a density of from 1.2 to 1.9 g/cm 3 and are used in the form of a coagulated mixture of emulsions of the tetrafluoroethylene polymers E) with emulsions of the graft polymers B).
  • Suitable tetrafluoroethylene polymers E) useable in powder form have particle sizes of, for example, from 100 to 1000 ⁇ m and densities of 2.0 g/cm 3 to 2.3 g/cm 3 .
  • tetrafluoroethylene polymers above all reduces or completely prevents dripping of the molten molding compound in the event of a fire.
  • their use in the form of a coagulated mixture improves the surface of moldings produced from the mixtures according to the invention, which is particularly important for the production of moldings of very large surface area and for production at very high processing temperatures.
  • an aqueous emulsion (latex) of a graft polymer B) having average latex particle sizes of from 0.1 to 2 ⁇ m and preferably from 0.2 to 0.6 ⁇ m is first mixed with a finely divided emulsion of a tetrafluoroethylene polymer E) in water having average particle sizes of from 0.05 to 20 ⁇ m and more especially from 0.08 to 10 ⁇ m.
  • Suitable tetrafluoroethylene polymer emulsions normally have solids contents of from 30 to 70% by weight and more especially from 50 to 60% by weight.
  • the emulsions of the graft polymers B) have solids contents of from 25 to 50% by weight and preferably from 30 to 45% by weight.
  • the ratio by weight of graft polymer B) to tetrafluoroethylene polymer E) in the emulsion mixture is from 95:5 to 60:40.
  • the emulsion mixture is then coagulated in known manner, for example by spray drying, freeze drying or coagulation by addition of inorganic or organic salts, acids, bases or organic water-miscible solvents, such as alcohols, ketones, preferably at temperatures in the range from 20° to 150° C. and more preferably at temperatures in the range from 50° to 100° C. If necessary, the product may be dried at 50° to 200° C. and preferably at 70° to 100° C.
  • Suitable tetrafluoroethylene polymer emulsions are commercial products and are marketed, for example, by Dupont as Teflon® 30N.
  • thermoplastic molding compounds according to the invention may contain other known additives for polycarbonates, graft polymers or for the thermoplastic polymers, such as stabilizers, pigments, flow aids, mold release agents, fillers and reinforcing materials and/or antistatic agents.
  • the filled or reinforced molding compounds may contain up to 60% by weight and preferably from 5 to 50% by weight, based on the filled or reinforced molding compound, of fillers and/or reinforcing materials.
  • Suitable reinforcing materials are glass fibers, carbon fibers, aramide fibers, etc.
  • Preferred reinforcing materials are glass fibers.
  • Preferred fillers which may also have a reinforcing effect are glass beads, mica, silicates, quartz, talcum, titanium dioxide, wollastonite.
  • the molding compounds according to the invention consisting of components A), B), D) and E) and, optionally, C) and/or optionally other known additives, such as stabilizers, pigments, flow aids, mold release agents, fillers and reinforcing materials and/or antistatic agents are prepared by mixing the respective constituents in known manner and then melt-compounding or melt-extruding the resulting mixture in standard units, such as internal kneaders or single-screw or twin-screw extruders, at temperatures in the range from 200° to 330° C. or by mixing solutions of the respective components in suitable organic solvents, for example in chlorobenzene, and concentrating the mixed solutions by evaporation in standard evaporation units, for example in evaporation extruders.
  • standard units such as internal kneaders or single-screw or twin-screw extruders
  • the present invention also relates to a process for the production of thermoplastic molding compounds consisting of components A), B), D) and E) and, optionally, component C), stabilizers, pigments, flow aids, fillers and reinforcing materials, mold release agents and/or antistatic agents, characterized in that components A), B), D) and E) and, optionally, component C), stabilizers, pigments, flow aids, fillers and reinforcing materials, mold release agents and/or antistatic agents, are mixed and melt-compounded or melt-extruded in conventional units at temperatures in the range from 200° to 330° C., component E) preferably being used in the form of a coagulated mixture with component B).
  • the individual constituents may be mixed in known manner either gradually or at the same time either at around 20° C. (room temperature) or even at a higher temperature.
  • the molding compounds according to the present invention may be used for the production of moldings of all kinds.
  • moldings may be produced by injection molding.
  • Examples of moldings which can be produced from the molding compounds according to the invention include housing components of all kinds, for example for domestic appliances, such as juice presses, coffee machines, mixers, for office machines or cover panels for the building industry and parts for the automotive sector.
  • they may be used in the field of electrical engineering where they show very good electrical properties.
  • Another form of processing is the production of moldings by deep drawing from prefabricated sheets or films.
  • particle size always means the average particle diameter d 50 , as determined by ultracentrifuge measurements in accordance with W. Scholtan et. al., Colloids, u. Z. Polymere 250 (1972), pages 782 to 796.
  • Tetrafluoroethylene polymer in the form of a coagulated mixture of an SAN graft polymer emulsion according to B) in water and a tetrafluoroethylene polymer emulsion in water.
  • the ratio by weight of graft polymer B) to the tetrafluoroethylene polymer E) in the mixture is 90% by weight to 10% by weight.
  • the tetrafluoroethylene polymer emulsion has a solids content of 60% by weight; the particle size is between 0.05 and 0.5 ⁇ m.
  • the SAN graft polymer emulsion has a solids content of 34% by weight and an average latex particle size of 0.4 ⁇ m.
  • the emulsion of the tetrafluoroethylene polymer was mixed with the emulsion of the SAN graft polymer B) and stabilized with 1.8% by weight, based on polymer solids, of phenolic antioxidants. At 85° to 95° C., the mixture was coagulated with an aqueous solution of MgSO 4 (Epsom salt) and acetic acid at pH 4 to 5, filtered and washed until substantially free from electrolyte, subsequently freed from most of the water by centrifugation and then dried at 100° C. to form a powder. This powder may then be compounded with the other components in the described units.
  • MgSO 4 Epsom salt
  • Components A), B), C), D) and E) were compounded in a Werner & Pfleiderer type ZSK 53 twin-screw extruder at a temperature of 240° C.
  • Moldings were produced in an injection molding machine at a temperature of 260° C.
  • the fire behavior of the test specimens was measured in accordance with UL-Subj. 94 V in test specimen thicknesses of 1.6 mm.
  • the UL-94 test is carried out as follows:
  • Material samples are molded into bars measuring 127 ⁇ 12.7 ⁇ 1.6 mm.
  • the bars are vertically mounted in such a way that the underneath of the test specimen is situated 304 mm above a strip of bandaging material.
  • Each test bar is individually ignited by two successive ignitions of 10 seconds duration, the burning properties are observed after each ignition and the test specimen is then evaluated.
  • a Bunsen burner having a 10 mm (3.8 inch) tall blue flame of natural gas with a heat content of 3.73 ⁇ 10 4 kJ/m 3 (1000 BUT per cubic foot) is used to ignite the test specimens.
  • the UL-94 V-0 classification encompasses the properties of materials described in the following which have been subjected to the UL-94 test.
  • the polycarbonate molding compounds in this class contain no test specimens which burn for longer than 10 seconds after each application of the test flame. They do not show a total flame time of more than 50 s during the two flame applications to each test specimen. They contain no test specimens which burn up completely to the retaining clip fastened to the upper end of the test specimen. They contain no test specimens which ignite the wadding arranged beneath the test specimen through burning droplets or particles. They also contain no test specimens which glow for longer than 30 seconds after removal of the test flame.
  • Notched impact strength was determined in accordance with DIN 53 453/ISO R 179 using test bars measuring 50 ⁇ 6 ⁇ 4 mm, the test bars being provided with a 2.7 mm deep V-shaped notch.
  • the oriterion used for stress crazing behavior was the reduction in impact strength (as determined on test bars measuring 50 ⁇ 6 ⁇ 4 mm in accordance with DIN 53 453/ISO R 179) after storage in a simulated fuel bath (mixture of 50% by weight toluene and 50% by weight iso-octane) at room temperature, the test specimens having been pre-extended on a circular template.
  • the values can be expected to be all the more unfavorable, i.e. the deteriorations in the properties can be expected to be greater, the longer the test specimens are stored in the test bath and the greater the pre-extension ⁇ x (in %).
  • n.b. The starting value for non-pre-extended test specimens not exposed to the test bath is n.b. ("not broken") for both Examples.
  • the impact strength of the Example according to the invention is reduced to a far lesser extent than in the case of the Comparison Example.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)

Abstract

The invention relates to polycarbonate molding compounds consisting of halogen-free polycarbonates, graft polymers, phosphorus compounds, tetrafluoroethylene polymers and, optionally, copolymers and/or, optionally, other additives known per se and a process for their production.

Description

This invention relates to high-impact, flame-retardant, thermoplastic polycarbonate molding compounds consisting of
A) 50 to 96.5 parts by weight, preferably 60 to 96 parts by weight and, more preferably, 70 to 95.5 parts by weight of one or more thermoplastic, halogen-free, aromatic polycarbonates based on diphenols corresponding to formula (II),
B) 3.5 to 25 parts by weight, preferably 4 to 15 parts by weight and, more preferably, 4.5 to 10 parts by weight of one or more halogen-free graft polymers of
B.1) 5 to 90 parts by weight, preferably 30 to 80 parts by weight, based on B., of a mixture of
B.1.1) 50 to 95% by weight styrene, α-methyl styrene, nucleus-substituted styrene, methyl methacrylate or mixtures thereof and
B.1.2) 50 to 5% by weight (meth)acrylonitrile, methyl methacrylate, n-butyl acrylate, t-butyl (meth)acrylate or mixtures thereof, on
B.2) 95 to 10 parts by weight, preferably 70 to 20 parts by weight, based on B), of a rubber having a glass temperature TG of ≦10° C. and
C) 0 to 40 parts by weight, preferably 1 to 30 parts by weight and, more preferably, 5 to 20 parts by weight of a halogen-free, thermoplastic copolymer of
C.1) 50 to 95% by weight styrene, methyl styrene, nucleus-substituted styrene, methyl methacrylate or mixtures thereof and
C.2) 50 to 5% by weight (meth)acrylonitrile, methyl methacrylate or mixtures thereof, the sum of the parts by weight of A)+B)+optionally C) having to amount to 100 parts by weight, and
D) 1 to 20 parts by weight, preferably 2 to 15 parts by weight and, more preferably, 3 to 12 parts by weight, based on 100 parts by weight of A)+B)+optionally C), of a halogen-free phosphorus compound corresponding to formula (I) ##STR1## in which R1, R2 and R3 independently of one another represent C1 -C8 alkyl or optionally alkyl-substituted C6 -C20 aryl and n=0 or 1, and
E) 0.05 to 5 parts by weight, preferably 0.1 to 1 part by weight and, more preferably, 0.1 to 0.5 part by weight, based on 100 parts by weight of A)+B)+optionally C), of a tetrafluoroethylene polymer having average particle sizes of from 0.05 to 1000 μm, a density of 1.2 to 2.3 g/cm3 and a fluorine content of 65 to 76% by weight, component E) preferably being used in the form of a coagulated mixture of emulsions of the tetrafluoroethylene polymers E) having an average particle size of 0.05 to 20μ and a density of 1.2 to 1.9 g/cm3 with emulsions of graft polymers B) and the ratio by weight of graft polymer B) to the tetrafluoroethylene polymer E) being from 95:5 to 60:40 and the content of addition quantities B), based on 100 parts by weight A)+B) and optionally C), being from 0.1 to 4.0 parts by weight and, optionally, effective quantities of standard stabilizers, pigments, flow aids, fillers and reinforcing materials, mold release agents and/or antistatic agents.
DE-OS 3 322 260 (Le A 22 391) describes flame-retardant thermoplastic molding compounds of
(a) 5 to 95 parts by weight polycarbonate,
(b) 5 to 95 parts by weight SAN graft polymer,
(c) 0 to 50 parts by weight of a thermoplastic polymer,
(d) optionally 3 to 15 parts by weight per 100 parts by weight (a)+(b)+(c) of an organic halogen compound,
(e) from 0.05 to 5 parts by weight per 100 parts by weight (a)+(b)+(c) of antimony trioxide, antimony carbonate, bismuth trioxide or bismuth carbonate,
(f) from 0.05 to 0.5 part by weight per 100 parts by weight of the sum of (a) to (f) of finely divided tetrafluoroethylene polymer.
Where antimony trioxide or antimony carbonate is used and where the tetrafluoroethylene polymer is specially incorporated by co-precipitation with components (b) and, optionally, (c), flame-retardant moldings having a good surface are obtained, achieving a rating of V - O for a thickness of 1.6 mm where additional halogen is present either through component (a) or through components (d) (cf. EP-PS 0 131 751).
DE-OS 3 430 234 (Le A 22 925) describes flame-resistant thermoplastic polymer mixtures containing special, halogen-free polycarbonates of 50 mol % to 100 mol % tetraalkylated bisphenol carbonate structural units, halogen-free styrene polymers and/or halogen-free graft polymers, halogen-free phosphate esters and, optionally, tetrafluoroethylene polymers.
EP-OS 0 174 493 (Le A 23 043-EP) describes thermoplastic molding compounds consisting of
A) 20 to 85 parts by weight of a thermoplastic aromatic polycarbonate,
B) 5 to 50 parts by weight of a graft polymer of
B.1) 5 to 90 parts by weight and preferably 30 to 80 parts by weight of a mixture of
B.1.1) 50 to 95% by weight styrene, α-methyl styrene, nucleus-substituted styrene, methyl methacrylate or mixtures thereof and
B.1.2) 50 to 5% by weight (meth)acrylonitrile, methyl methacrylate, maleic anhydride, N-substituted maleic imide or mixtures thereof, on
B.2) 95 to 10 parts by weight and preferably 70 to 20 parts by weight of a rubber having a glass temperature TG of ≦10° C.,
C) 5 to 70 parts by weight of a thermoplastic copolymer of
C.1) 50 to 95% by weight styrene, α-methyl styrene, nucleus-substituted styrene, methyl methacrylate or mixtures thereof and
C.2) 50 to 5% by weight (meth)acrylonitrile, methyl methacrylate, maleic anhydride, N-substituted maleic imide or mixtures thereof and, optionally,
D) 3 to 15 parts by weight of a low molecular weight or high molecular weight halogen compound, more especially a bromine compound, based on 100 parts by weight of A)+B)+C) and, optionally, D), the halogen content arising out of components A)+D) having to amount to between 3% by weight and 10% by weight, based on the total weight of components A)+D), characterized in that they additionally contain
E) 1 to 15 parts by weight and preferably 2 to 12 parts by weight of a phosphorus compound corresponding to formula (I) ##STR2## in which R1, R2 and R3 independently of one another represent an optionally halogenated C1 -C8 alkyl or an optionally halogenated C6 -C20 aryl and n=0 or 1 and
F) from 0.05 to 1 part by weight and more especially from 0.1 to 0.5 part by weight of a tetrafluoroethylene polymer having an average particle size of from 0.05 to 20 μm and a density of from 1.2 to 1.9 g/cm3, the parts by weight of components E) and F) being based on 100 parts by weight of the sum of components A)+B)+C) and, optionally, D) and component F) being used in the form of a coagulated mixture of emulsions of the tetrafluoroethylene polymers F) with emulsions of additional quantities of graft polymers B) of at most 4 parts by weight, but at least 0.1 part by weight, based on 100 parts by weight of the sum of components A)+B)+C) and, optionally, D).
It was found that UL-94 ratings of V-O for a thickness of 1.6 mm were only obtained in the presence of component D) and/or where halogenated polycarbonate was used as component A).
It has now been found that, in contrast to the teaching of EP-OS 0 174 493, a UL-94 rating of V-O is achieved with the molding compounds according to the invention, even in the absence of halogen (Cl, Br) compounds. It had been expected that it would not be possible to achieve a rating of V-O for a thickness of 1.6 mm through the presence of additional graft polymers in addition to the quantity of 0.1 to 4 parts by weight present through the co-precipitation of Teflon.
DE-OS 3 521 388 (Le A 23 877) describes thermoplastic flame-resistant molding compounds containing halogen-free polycarbonates, copolymers of styrenes with maleic anhydride, phosph(on)ate esters, tetrafluoroethylene polymers and 0.1 to 3 parts by weight graft polymers, the graft polymers again having been co-precipitated with the tetrafluoroethylene polymers. Although these molding compounds achieve a V-O rating for a thickness of 1.6 mm, their toughness, flow line strength and resistance to stress crazing are inadequate for numerous applications.
DE-OS 3 523 314 (Le A 23 940) describes high-impact, flame-retardant molding compounds of halogen-free polycarbonates, halogen-free styrene-acrylonitrile copolymers, phosphorus compounds, tetrafluoroethylene polymers and 0.1 to 3 parts by weight graft polymers, the graft polymers again having been co-precipitated with the tetrafluoroethylene polymers.
However, the toughness, flow line strength and resistance to stress crazing of the molding compounds according to DE-OS 3 523 314 is inadequate for certain applications, particularly in the case of complicated, flame-proofed moldings, such as housing components, where design-related openings, webs and the like call for as high a level of the above-mentioned properties as possible.
DE-OS 3 545 609 (Le A 24 039) describes halogen-free; substantially non-inflammable molding compounds consisting of
A) 40 to 95 parts by weight, based on 100 parts by weight A)+B)+C), of a thermoplastic, halogen-free aromatic polycarbonate,
B) 5 to 30 parts by weight, based on 100 parts by weight of A)+B)+C), of a halogen-free "ABS" graft polymer obtainable from 20 to 90% by weight of a mixture of
a) 95 to 50% by weight styrene, p-methyl styrene, α-methyl styrene or mixtures thereof and
b) 5 to 50% by weight acrylonitrile and/or methacrylonitrile on 80 to 10% by weight of a diene rubber,
C) 10 to 30 parts by weight, based on 100 parts by weight A)+B)+C), of a halogen-free, statistical copolymer of
C.1) 5 to 30% by weight maleic anhydride and
C.2) 95 to 70% by weight styrene, α-methyl styrene, nucleus-alkylated styrenes or mixtures of these styrenes,
D) 1 to 20 parts by weight, based on 100 parts by weight of the total weight of A)+B)+C), of a halogen-free phosphorus compound corresponding to formula (I) ##STR3## in which R1, R2 and R3 independently of one another represent C1 -C8 alkyl or optionally alkyl-substitute C6 -C20 aryl and n=0 or 1; two of the indices n may also be 1 and the third 0,
E) 0.05 to 5 parts by weight, based on 100 parts by weight of the total weight of A)+B)+C), of a tetrafluoroethylene polymer and, optionally,
F) stabilizers, pigments, flow aids, mold release agents and/or antistatic agents.
However, molding compounds of the type in question have the disadvantage of a narrower processing scope and lower flow line strength than the molding compounds according to the invention.
DE-OS 3 628 904 (Le A 24 683) describes high-impact flame-retardant polycarbonate molding compounds consisting of
A) 60 to 90 parts by weight of a halogen-free polydiorganosiloxane-polycarbonate block copolymer having an average molecular weight Mw of 10,000 to 200,000 and a content of aromatic carbonate structural units of 75 to 99% by weight and a content of diorganosiloxane units of 25 to 1.0% by weight, the block copolymers being produced from α,ω-bis-hydroxyaryloxy-terminated polydiorganosiloxanes with a degree of polymerization Pn of from 5 to 100,
B) 10 to 40 parts by weight of a halogen-free, thermoplastic copolymer of 50 to 95% by weight styrene, α-methyl styrene, nucleus-substituted styrene or mixtures thereof and 5 to 50% by weight (meth)acrylonitrile,
C) 1 to 20 parts by weight, based on 100 parts by weight of the total weight of A) and B), of a halogen-free phosphorus compound corresponding to formula (I) ##STR4## in which R1, R2 and R3 independently of one another represent C1 -C8 alkyl or optionally alkyl-substituted C6 -C20 aryl and n=0 or 1, and
D) 0.05 to 5 parts by weight, again based on 100 parts by weight of the total weight of A) and B), of a tetrafluoroethylene polymer having a density of 2.0 to 2.3 g/cm3 and a particle size of 100 to 1000 μm.
DE-OS 3 629 546 (Le-A 24 695) describes high-impact flame-retardant molding compounds containing
A) 60 to 90 parts by weight of a halogen-free polydiorganosiloxane-polycarbonate block copolymer having an average molecular weight Mw of 10,000 to 20,000 and a content of aromatic carbonate structural units of 75 to 99% by weight and a content of diorganosiloxane units of 25 to 1.0% by weight, the block copolymers being produced from α,ω-bis-hydroxyaryloxy-terminated polydiorganosiloxanes with a degree of polymerization Pn of 5 to 100,
B) 10 to 40 parts by weight of a halogen-free, thermoplastic copolymer of 50 to 95% by weight styrene, α-methyl styrene, nucleus-substituted styrene or mixtures thereof and 5 to 50% by weight (meth)acrylonitrile,
C) 1 to 20 parts by weight, based on 100 parts by weight of the total weight of A) and B), of a halogen-free phosphorus compound corresponding to formula (I) ##STR5## in which R1, R2 and R3 independently of one another represent C1 -C8 alkyl or optionally alkyl-substituted C6 -C20 aryl and n=0 or 1 and
D) 0.05 to 5 parts by weight, based on 100 parts by weight of the total weight of A) and B), of a tetrafluoroethylene polymer having average particle sizes of 0.05 to 20 μm and a density of 1.2 to 1.9 g/cm3, component D) being used in the form of a coagulated mixture of emulsions of the tetrafluoroethylene polymers D) with emulsions of at most 3 parts by weight, but at least 0.1 part by weight, based on 100 parts by weight of the sum of components A) and B), of graft polymers
E) of 5 to 90 parts by weight of a mixture of
E.1.1) 50 to 95 parts by weight styrene, α-methyl styrene, nucleus-substituted styrene, methyl methacrylate or mixtures thereof and
E.1.2) 50 to 5% by weight (meth)acrylonitrile, methyl methacrylate, maleic anhydride, N-substituted maleic imide or mixtures thereof, on
E.2) 95 to 100 parts by weight of a rubber having a glass temperature TG of ≦10° C.,
and the ratio by weight of graft polymer E) to the tetrafluoroethylene polymer D) being from 95:5 to 60:40.
However, the molding compounds according to DE-OS 3 4 and DE-OS 3 629 546 show inadequate resistance to stress crazing.
The technical advantage of the molding compounds according to the invention lies in the extremely advantageous combination of toughness, resistance to stress crazing and flame resistance, the latter being achieved without any halogen (Br, Cl) and metal compounds.
Thermoplastic, halogen-free, aromatic polycarbonates of component A) suitable for use in accordance with the invention are those based on diphenols corresponding to formula (II) ##STR6## in which A is a single bond, C1 -C5 alkylene, C2 -C5 alkylidene, C5 -C6 cycloalkylidene, --S-- or --SO2 --.
Suitable diphenols corresponding to formula (II) are, for example, hydroquinone, resorcinol, 4,4'-dihydroxydiphenyl, 2,2-bis-(4-hydroxyphenyl)-propane, 2,4-bis-(4-hydroxyphenyl)-2-methyl butane or 1,1-bis-(4-hydroxyphenyl)cyclohexane.
Preferred diphenols corresponding to formula (II) are 2,2-bis-(4-hydroxyphenyl)-propane and 1,1-bis-(4-hydroxyphenyl)-cyclohexane.
The diphenols corresponding to formula (II) are either known from the literature or may be produced by methods known from the literature.
The production of the polycarbonates of component A) suitable for use in accordance with the invention is known from the literature and may be carried out, for example, with phosgene by the interfacial process or with phosgene by the homogeneous-phase process (so-called pyridine process), the particular molecular weight to be established being obtained in known manner through a corresponding quantity of known chain terminators. Suitable chain terminators are, for example, monophenols, such as phenol itself, p-cresol, p-tert.-butylphenol and p-isooctylphenol.
The polycarbonates of component A) suitable for use in accordance with the invention have average molecular weights (Mw, as measured for example by ultracentrifugation or by scattered light measurement) of from 10,000 to 200,000 and preferably from 20,000 to 80,000.
The polycarbonates of component A) suitable for use in accordance with the invention are both homopolycarbonates and also copolycarbonates.
The polycarbonates of component A) suitable for use in accordance with the invention may be branched in known manner, preferably through the incorporation of 0.05 to 2.0 mol %, based on the sum of the diphenols used, of trifunctional or more than trifunctional compounds, for example those containing three or more than three phenolic OH groups.
In the context of the invention, "halogen-free polycarbonates" are understood to be polycarbonates of halogen-free diphenols, halogen-free chain terminators and, optionally, halogen-free branching agents, the content of small quantities (ppm) of hydrolyzable chlorine, resulting for example from the production of the polycarbonates with phosgene by the interfacial process, not counting as "halogen-containing" in the context of the invention. Polycarbonates such as these having ppm contents of hydrolyzable chlorine are halogen-free polycarbonates in the context of the invention.
Rubbers suitable for the production of the halogen-free graft polymers B) are, in particular, polybutadiene, butadiene/styrene copolymers (both also copolymerized with up to 30% by weight, based on the weight of the rubber, of a lower alkyl ester of acrylic or methacrylic acid, such as methyl methacrylate, ethyl acrylate, methyl acrylate or ethyl methacrylate), polyisoprene, alkyl acrylate rubbers (of C1 -C8 alkyl acrylates, particularly ethyl, butyl, ethyl hexyl acrylate). The alkyl acrylate rubbers may optionally contain up to 30% by weight, based on the weight of the rubber, of such monomers as vinyl acetate, acrylonitrile, styrene, methyl methacrylate and/or vinyl ethers in copolymerized form and also relatively small quantities, preferably up to 5% by weight, based on the weight of the rubber, of crosslinking, ethylenically unsaturated monomers. Crosslinking agents such as these are, for example, alkylenediol di-(meth)-acrylates, polyester di-(meth)-acrylates, divinylbenzene, trivinylbenzene, triallyl cyanurate, allyl (meth)acrylate, butadiene or isoprene. Suitable acrylate rubbers are those which contain a crosslinked diene rubber of one or more conjugated dienes and, optionally, an ethylenically unsaturated monomer, such as styrene and/or acrylonitrile, as core. Other suitable rubbers are, for example, EPDM rubbers, i.e. rubbers of ethylene, propylene and an unconjugated diene, and also silicone rubbers.
Preferred rubbers for the production of the graft polymers B) are diene and alkyl acrylate rubbers.
The rubbers are present in the graft polymers B) in the form of at least partly crosslinked particles having an average particle size from 0.09 to 5 μm and more especially from 0.1 to 1 μm. The graft polymers B) are produced by radical graft copolymerization of the monomer mixtures defind at the beginning of B.1.1) and B.1.2) in the presence of the rubbers B.2) to be grafted and are all known. Preferred production processes for the graft polymers B) are emulsion, solution, bulk or suspension polymerization. Particularly preferred graft polymers B) are the so-called ABS polymers. Nucleus-substituted styrenes are understood to be nucleus-alkylated styrenes, such as for example p-methyl styrene.
Copolymers of component C) are often formed as secondary products in the graft polymerization for the production of component B), particularly when large quantities of monomers are grafted onto small quantities of rubber.
The quantity of copolymer C) to be used in accordance with the invention does not include these secondary graft polymerization products.
The copolymers of component C) are resin-like, thermoplastic and rubber-free. Particularly preferred copolymers C) are those of styrene with acrylonitrile and, optionally, with methyl methacrylate, of α-methyl styrene with acrylonitrile and, optionally, with methyl methacrylate or of styrene and α-methyl styrene with acrylonitrile and, optionally, with methyl methacrylate.
Particularly preferred ratios by weight in the thermoplastic copolymer C) are 60 to 80% by weight C.1) and 40 to 20% by weight C.2).
The styrene-acrylonitrile copolymers of component C) are known and may be produced by radical polymerization, more especially by emulsion, suspension, solution or bulk polymerization. The copolymers of component C) preferably have molecular weights M (weight average, as determined by light scattering or sedimentation) of from 15,000 to 200,000.
The halogen-free phosphorus compounds of component D) suitable for use in accordance with the invention are generally known (cf. for example Ullmann, Enzyklopadie der technischen Chemie, Vol. 18, pages 301 et seq., 1979; Houben-Weyl, Methoden der Organischen Chemie, Vol. 12/1, page 43; Beilstein, Vol. 6, page 177).
Phosphorus compounds of component D), formula (I), suitable for use in accordance with the invention are, for example, triphenylphosphate, tricresylphosphate, diphenyl-2-ethyl cresylphosphate, tri-(isopropylphenyl)-phosphate, methylphosphonic acid diphenyl ester, phenyl phosphonic acid diethyl ester, diphenyl cresylphosphate and tributylphosphate.
The tetrafluoroethylene polymers of component e) suitable for use in accordance with the invention are polymers having fluorine contents of from 65 to 76% by weight and preferably from 70 to 76% by weight. Examples of such polymers are polytetrafluoroethylene, tetrafluoroethylene-hexafluoropropylene copolymers or tetrafluoroethylene copolymers containing small quantities of fluorine-free, copolymerizable, ethylenically unsaturated monomers. The polymers are known and may be produced by known methods, for example by polymerization of tetrafluoroethylene in aqueous medium with a catalyst forming free radicals, for example sodium, potassium or ammonium peroxydisulfate, under pressures of 7 to 71 kg/cm2 and at temperatures of from 0° to 200° C. and preferably at temperatures of 20° to 100° C. (For further particulars, cf. for example U.S. Pat. No. 2,393,967.) Depending on the form in which they are used, these materials may have a density of 1.2 to 2.3 g/cm3 and an average particle size of 0.05 to 1000 μm.
According to the invention, preferred polytetrafluoroethylenes have average particle sizes from 0.05 to 20 μm and preferably from 0.08 to 10 μm and a density of from 1.2 to 1.9 g/cm3 and are used in the form of a coagulated mixture of emulsions of the tetrafluoroethylene polymers E) with emulsions of the graft polymers B).
Suitable tetrafluoroethylene polymers E) useable in powder form have particle sizes of, for example, from 100 to 1000 μm and densities of 2.0 g/cm3 to 2.3 g/cm3.
The use of tetrafluoroethylene polymers above all reduces or completely prevents dripping of the molten molding compound in the event of a fire. In addition, their use in the form of a coagulated mixture improves the surface of moldings produced from the mixtures according to the invention, which is particularly important for the production of moldings of very large surface area and for production at very high processing temperatures.
To produce a coagulated mixture of B) and E), an aqueous emulsion (latex) of a graft polymer B) having average latex particle sizes of from 0.1 to 2 μm and preferably from 0.2 to 0.6 μm is first mixed with a finely divided emulsion of a tetrafluoroethylene polymer E) in water having average particle sizes of from 0.05 to 20 μm and more especially from 0.08 to 10 μm. Suitable tetrafluoroethylene polymer emulsions normally have solids contents of from 30 to 70% by weight and more especially from 50 to 60% by weight. The emulsions of the graft polymers B) have solids contents of from 25 to 50% by weight and preferably from 30 to 45% by weight.
The ratio by weight of graft polymer B) to tetrafluoroethylene polymer E) in the emulsion mixture is from 95:5 to 60:40. The emulsion mixture is then coagulated in known manner, for example by spray drying, freeze drying or coagulation by addition of inorganic or organic salts, acids, bases or organic water-miscible solvents, such as alcohols, ketones, preferably at temperatures in the range from 20° to 150° C. and more preferably at temperatures in the range from 50° to 100° C. If necessary, the product may be dried at 50° to 200° C. and preferably at 70° to 100° C.
Suitable tetrafluoroethylene polymer emulsions are commercial products and are marketed, for example, by Dupont as Teflon® 30N.
The thermoplastic molding compounds according to the invention may contain other known additives for polycarbonates, graft polymers or for the thermoplastic polymers, such as stabilizers, pigments, flow aids, mold release agents, fillers and reinforcing materials and/or antistatic agents.
The filled or reinforced molding compounds may contain up to 60% by weight and preferably from 5 to 50% by weight, based on the filled or reinforced molding compound, of fillers and/or reinforcing materials. Suitable reinforcing materials are glass fibers, carbon fibers, aramide fibers, etc. Preferred reinforcing materials are glass fibers. Preferred fillers which may also have a reinforcing effect are glass beads, mica, silicates, quartz, talcum, titanium dioxide, wollastonite.
The molding compounds according to the invention, consisting of components A), B), D) and E) and, optionally, C) and/or optionally other known additives, such as stabilizers, pigments, flow aids, mold release agents, fillers and reinforcing materials and/or antistatic agents are prepared by mixing the respective constituents in known manner and then melt-compounding or melt-extruding the resulting mixture in standard units, such as internal kneaders or single-screw or twin-screw extruders, at temperatures in the range from 200° to 330° C. or by mixing solutions of the respective components in suitable organic solvents, for example in chlorobenzene, and concentrating the mixed solutions by evaporation in standard evaporation units, for example in evaporation extruders.
Accordingly, the present invention also relates to a process for the production of thermoplastic molding compounds consisting of components A), B), D) and E) and, optionally, component C), stabilizers, pigments, flow aids, fillers and reinforcing materials, mold release agents and/or antistatic agents, characterized in that components A), B), D) and E) and, optionally, component C), stabilizers, pigments, flow aids, fillers and reinforcing materials, mold release agents and/or antistatic agents, are mixed and melt-compounded or melt-extruded in conventional units at temperatures in the range from 200° to 330° C., component E) preferably being used in the form of a coagulated mixture with component B).
The individual constituents may be mixed in known manner either gradually or at the same time either at around 20° C. (room temperature) or even at a higher temperature.
The molding compounds according to the present invention may be used for the production of moldings of all kinds. In particular, moldings may be produced by injection molding. Examples of moldings which can be produced from the molding compounds according to the invention include housing components of all kinds, for example for domestic appliances, such as juice presses, coffee machines, mixers, for office machines or cover panels for the building industry and parts for the automotive sector. In addition, they may be used in the field of electrical engineering where they show very good electrical properties.
Another form of processing is the production of moldings by deep drawing from prefabricated sheets or films.
In the context of the invention, particle size always means the average particle diameter d50, as determined by ultracentrifuge measurements in accordance with W. Scholtan et. al., Colloids, u. Z. Polymere 250 (1972), pages 782 to 796.
EXAMPLES 1. Components used
A) Polycarbonate of 2,2-bis-(4-hydroxyphenyl)-propane (bisphenol A) having a relative solution viscosity ηrel of 1.31, as measured in methylene chloride at 23° C. and at a concentration of 0.5% by weight.
B) SAN graft polymer of 50% by weight of a styrene/acrylonitrile mixture (ratio by weight 72:28) on 50% by weight of a particulate polybutadiene having an average particle size (d50) of 0.4 μm, obtained by emulsion polymerization.
C) Styrene/acrylonitrile copolymer in which the ratio of styrene to acrylonitrile is 72:28 and which has a viscosity number [η] of 0.55 dl/g (as measured in dimethylformamide at 20° C.).
D) Triphenylphosphate
E) Tetrafluoroethylene polymer in the form of a coagulated mixture of an SAN graft polymer emulsion according to B) in water and a tetrafluoroethylene polymer emulsion in water. The ratio by weight of graft polymer B) to the tetrafluoroethylene polymer E) in the mixture is 90% by weight to 10% by weight. The tetrafluoroethylene polymer emulsion has a solids content of 60% by weight; the particle size is between 0.05 and 0.5 μm. The SAN graft polymer emulsion has a solids content of 34% by weight and an average latex particle size of 0.4 μm.
Production of E
The emulsion of the tetrafluoroethylene polymer was mixed with the emulsion of the SAN graft polymer B) and stabilized with 1.8% by weight, based on polymer solids, of phenolic antioxidants. At 85° to 95° C., the mixture was coagulated with an aqueous solution of MgSO4 (Epsom salt) and acetic acid at pH 4 to 5, filtered and washed until substantially free from electrolyte, subsequently freed from most of the water by centrifugation and then dried at 100° C. to form a powder. This powder may then be compounded with the other components in the described units.
2. Production and testing of the molding compounds according to the invention
Components A), B), C), D) and E) were compounded in a Werner & Pfleiderer type ZSK 53 twin-screw extruder at a temperature of 240° C.
Moldings were produced in an injection molding machine at a temperature of 260° C.
The fire behavior of the test specimens was measured in accordance with UL-Subj. 94 V in test specimen thicknesses of 1.6 mm. The UL-94 test is carried out as follows:
Material samples are molded into bars measuring 127×12.7×1.6 mm. The bars are vertically mounted in such a way that the underneath of the test specimen is situated 304 mm above a strip of bandaging material. Each test bar is individually ignited by two successive ignitions of 10 seconds duration, the burning properties are observed after each ignition and the test specimen is then evaluated. A Bunsen burner having a 10 mm (3.8 inch) tall blue flame of natural gas with a heat content of 3.73×104 kJ/m3 (1000 BUT per cubic foot) is used to ignite the test specimens.
The UL-94 V-0 classification encompasses the properties of materials described in the following which have been subjected to the UL-94 test. The polycarbonate molding compounds in this class contain no test specimens which burn for longer than 10 seconds after each application of the test flame. They do not show a total flame time of more than 50 s during the two flame applications to each test specimen. They contain no test specimens which burn up completely to the retaining clip fastened to the upper end of the test specimen. They contain no test specimens which ignite the wadding arranged beneath the test specimen through burning droplets or particles. They also contain no test specimens which glow for longer than 30 seconds after removal of the test flame.
Other UL-94 classifications apply to specimens which are less flame-retardant and self-extinguishing and which release flaming droplets or particles. These are the UL-94 V-1 and V-2 classifications. F. stands for "failed" and is the classification given to specimens which continue burning for 30 seconds.
Notched impact strength was determined in accordance with DIN 53 453/ISO R 179 using test bars measuring 50×6×4 mm, the test bars being provided with a 2.7 mm deep V-shaped notch.
The oriterion used for stress crazing behavior was the reduction in impact strength (as determined on test bars measuring 50×6×4 mm in accordance with DIN 53 453/ISO R 179) after storage in a simulated fuel bath (mixture of 50% by weight toluene and 50% by weight iso-octane) at room temperature, the test specimens having been pre-extended on a circular template. In the case of materials vulnerable to stress crazing, the values can be expected to be all the more unfavorable, i.e. the deteriorations in the properties can be expected to be greater, the longer the test specimens are stored in the test bath and the greater the pre-extension εx (in %). The starting value for non-pre-extended test specimens not exposed to the test bath is n.b. ("not broken") for both Examples. For Example 1 according to the invention (see Table 1 below), a reduction in impact strength n.b. to 90 kJ/m2 is observed after storage for 7 days in the test bath at εx =1%, a reduction to 85 kJ/m2 being observed after storage for 30 days at εx =1%. By contrast, Comparison Example 2 (Table 2 below) shows a reduction in impact strength n.b. to as low as 15 kJ/m2 after only 7 days' storage in the test bath at εx =0.6%, a reduction to 10 kJ/m2 being observed after storage for 30 days under the same conditions. Despite the greater pre-extension εx, the impact strength of the Example according to the invention is reduced to a far lesser extent than in the case of the Comparison Example. As Table 1 below shows, the molding compounds according to the invention also show distinctly higher notched impact strength for the same flame resistance.
              TABLE 1                                                     
______________________________________                                    
Composition and properties of the molding compounds                       
        Components  Notched impact                                        
        (parts by weight)                                                 
                    strength    UL 94 V                                   
Example   A     B     C   D   E   [kJ/m.sup.2 ]                           
                                            [1.6 mm]                      
______________________________________                                    
1         65    5     15  12  3   10.7      VO                            
(invention)                                                               
2         65    --    20  12  3    3.9      VO                            
(Comparison)                                                              
______________________________________                                    

Claims (20)

We claim:
1. Thermoplastic molding compounds consisting of
A) 50 to 96.5 parts by weight of one or more thermoplastic, halogen-free, aromatic polycarbonates based on diphenols corresponding to ##STR7## wherein A is a single bond, C1-5 alkylene, C2-5 alkylidene, C5-6 cycloalkylidene, --S-- or SO2
B) 3.5 to 25 parts by weight of one or more halogen-free graft polymers of
B.1) 5 to 90 parts by weight, based on B), of a mixture of
B.1.1) 50 to 95% by weight styrene, α-methyl styrene, nucleus-substituted styrene, methyl methacrylate or mixtures thereof and
B.1.2) 50 to 5% by weight (meth)acrylonitrile, methyl methacrylate, n-butyl acrylate, t-butyl (meth)acrylate or mixtures thereof on
B.2) 95 to 10 parts by weight, based on B), of a rubber having a glass temperature TG of ≦10° C. selected from the group consisting of butadiene, butadiene/styrene copolymer, polyisoprene, EPDM and silicone rubbers, and
C) 0 to 40 parts by weight of a halogen-free, thermoplastic copolymer of
C.1) 50 to 95% by weight styrene, α-methyl styrene, nucleus-substituted styrene, methyl methacrylate or mixtures thereof,
C.2) 50 to 5% by weight (meth)acrylonitrile, methyl methacrylate or mixtures thereof, the sum of the parts by weight of A)+B)+optionally C) having to amount to 100 parts by weight, and
D) 1 to 20 parts by weight, based on 100 parts by weight of A)+B)+optionally C), of a halogen-free phosphorus compound corresponding to ##STR8## in which R1, R2 and R3 independently of one another represent C1 -C8 alkyl or C6 -C20 aryl and n=0 or 1, and
E) 0.05 to 5 parts by weight, based on 100 parts by weight of A)+B)+optionally C), of a tetrafluoroethylene polymer having average particle sizes of 0.05 to 1000 μm, a density of 1.2 to 2.3 g/cm3 a fluorine content of 65 to 76% by weight.
2. Molding compounds as claimed in claim 1, characterized in that component A) is present in quantities of 60 to 96 parts by weight and component B) in quantities of 4 to 15 parts by weight.
3. Molding compounds as claimed in claim 1, characterized in that component A) is present in quantities of 70 to 95.5 parts by weight and component B) in quantities of 4.5 to 10 parts by weight.
4. Molding compounds as claimed in claim 1, characterized in that component C) is present in quantities of 1 to 30 parts by weight.
5. Molding compounds as claimed in claim 4, characterized in that component C) is present in quantities of 5 to 20 parts by weight.
6. Molding compounds as claimed in claim 1, characterized in that component D) is present in quantities of 2 to 15 parts by weight.
7. Molding compounds as claimed in claim 6, characterized in that component D) is present in quantities of 3 to 12 parts by weight.
8. Molding compounds as claimed in claim 1 , characterized in that component E) is present in quantities of 0.1 to 1 part by weight.
9. Molding compounds as claimed in claim 8, characterized in that component E) is present in quantities of 0.1 to 0.5 part by weight.
10. Molding compounds as claimed in claim 1, characterized in that component B) is synthesized from 30 to 80 parts by weight B.1 and 70 to 20 parts by weight B.2.
11. Molding compounds as claimed in claim 1 characterized in that component E) is used in the form of a coagulated mixture of emulsions of the tetrafluoroethylene polymers E) having an average particle size of 0.05 to 20 μm and a density of 1.2 to 1.9 g/cm3 with emulsions of graft polymers B), the ratio by weight of graft polymer B) to the tetrafluoroethylene polymer E) is from 95:5 to 60:40 and the content of additional quantities B), based on 100 parts by weight A)+B)+optionally C), is between 0.1 and 4.0 parts by weight.
12. Molding compounds as claimed in claim 1 characterized in that they contain effective quantities of at least one additive selected from the group consisting of stabilizers, pigments, flow aids, fillers and reinforcing materials, mold release agents and/or antistatic agents.
13. Molding compounds as claimed in claim 12, characterized in that they contain as reinforcing materials up to 60% by weight, based on the molding compound to be reinforced, of glass fibers.
14. A process for the production of the molding compounds claimed in claim 1, characterized in that components A), B), D), E) and, optionally, C) are mixed in known manner and the resulting mixture is melt-compounded or melt-extruded in standard units at temperatures in the range from 200° to 330° C.
15. The process of claim 14 characterized in that at least one additive selected from the group consisting of stabilizers, pigments, flow adds, fillers and reinforcing materials, mold release agents and anti-static agents is also incorporated.
16. A thermoplastic molding compound consisting of
A) 50 to 96.5 parts by weight of one or more thermoplastic, halogen-free aromatic polycarbonates based on diphenols corresponding to ##STR9## wherein A is a single bond, C1-5 alkylene, C2-5 alkylidene, C5-6 cycloalkylidene, --S-- or --SO2
B) 4.5 to 10 parts by weight of one or more halogen-free graft polymers of
B.1) 5 to 90 parts by weight, based on B), of a mixture of
B.1.1) 50 to 95% by weight styrene, α-methyl styrene, nucleus-substituted styrene, methyl methacrylate or mixtures thereof and
B.1.2) 50 to 5% by weight (meth)acrylonitrile, methyl methacrylate, n-butyl acrylate, t-butyl (meth)acrylate or mixtures thereof on
B.2) 95 to 10 parts by weight, based on B), of a rubber having a glass temperature Tg of ≦10° C. selected from the group consisting of butadiene, butadiene/styrene copolymer, polyisoprene, EPDM and silicone rubbers, and
C) 0 to 40 parts by weight of a halogen-free, thermoplastic copolymer of
C1) 50 to 95% by weight styrene, α-methyl styrene, nucleus-substituted styrene, methyl methacrylate or mixtures thereof, and
C2) 50 to 5% by weight (meth)acrylonitrile, methyl methacrylate or mixtures thereof,
the sum of the parts by weight of A)+B)+optionally C) having to amount to 100 parts by weight, and
D) 1 to 20 parts by weight, based on 100 parts by weight of A)+B)+optionally C), of a halogen-free phosphorus compound corresponding to ##STR10## in which R1, R2 and R3 independently of one another represent C1 -C8 alkyl or C6 -C20 aryl and n=0 or 1, and
E) 0.05 to 5 parts by weight, based on 100 parts by weight of A)+B)+optionally C), of a tetrafluoroethylene polymer having average particle sizes of 0.05 to 1000 μm, a density of 1.2 to 2.3 g/cm3 and a fluorine content of 65 to 76% by weight.
17. A thermoplastic molding compound consisting of
A) 60 to 96 parts by weight of one or more thermoplastic, halogen-free aromatic polycarbonates based on diphenols corresponding to ##STR11## wherein A is a single bond, C1-5 alkylene, C2-5 alkylidene, C5-6 cycloalkylidene, --S-- or SO2
B) 4.0 to 15 parts by weight, of one or more halogen-free graft polymers of
B.1) 5 to 90 parts by weight, based on B), of a mixture of
B.1.1.) 50 to 95% by weight styrene, α-methyl styrene, nucleus-substituted styrene, methyl methacrylate or mixture thereof and
B.1.2) 50 to 5% by weight (meth)acrylonitrile, methyl methacrylate, n-butyl acrylate, t-butyl (meth) acrylate or mixtures thereof on
B.2) 95 to 10 parts by weight, based on B), of a rubber having a glass temperature Tg of ≦10° C. selected from the group consisting of butadiene, butadiene/styrene copolymer, polyisoprene, EPDM and silicone rubbers, and
C) 0 to 40 parts by weight of a halogen-free, thermoplastic copolymer of
C.1) 50 to 95% by weight styrene, α-methyl styrene, nucleus-substituted styrene, methyl methacrylate or mixtures thereof, and
C.2) 50 to 5% by weight (meth)acrylonitrile, methyl methacrylate or mixtures thereof,
the sum of the parts by weight of A)+B)+optionally C) having to amount to 100 parts by weight, and
D) 1 to 20 parts by weight, based on 100 parts by weight of A)+B)+optionally B), of a halogen-free phosphorus compound corresponding to ##STR12## in which R1, R2 and R3 independently of one another represent C1 -C8 alkyl or C6 -C20 aryl and n=0 to 1,
E) 0.05 to 5 parts by weight, based on 100 parts by weight of A)+B)+optionally C), of a tetrafluoroethylene polymer having average particle sizes of 0.05 to 1000 μm, a density of 1.2 to 2.3 g/cm3 and a fluorine content of 65 to 76% by weight.
18. The compound of claim 1 wherein said rubber is butadiene or butadiene/styrene copolymer.
19. The compound of claim 16 wherein said rubber is butadiene or butadiene/styrene copolymer.
20. The compound of claim 17 wherein said rubber is butadiene or butadiene/styrene copolymer.
US07/355,957 1988-06-04 1989-05-23 Flame-retardant, high-impact polycarbonate molding compounds Expired - Lifetime US5061745A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3819081 1988-06-04
DE3819081A DE3819081A1 (en) 1988-06-04 1988-06-04 FLAME-RESISTANT, IMPACT TOOL POLYCARBONATE MOLDS

Publications (1)

Publication Number Publication Date
US5061745A true US5061745A (en) 1991-10-29

Family

ID=6355881

Family Applications (1)

Application Number Title Priority Date Filing Date
US07/355,957 Expired - Lifetime US5061745A (en) 1988-06-04 1989-05-23 Flame-retardant, high-impact polycarbonate molding compounds

Country Status (5)

Country Link
US (1) US5061745A (en)
EP (1) EP0345522B1 (en)
JP (1) JPH0670177B2 (en)
DE (2) DE3819081A1 (en)
ES (1) ES2120943T3 (en)

Cited By (121)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5219907A (en) * 1991-09-27 1993-06-15 Basf Aktiengesellschaft Flameproofed molding composition
US5266618A (en) * 1991-05-28 1993-11-30 Denki Kagaku Kogyo Kabushiki Kaisha Flame-retardant resin composition
US5272193A (en) * 1991-07-12 1993-12-21 Bayer Aktiengesellschaft Thermoplastic polycarbonate moulding compounds with flame-resistant properties
US5276256A (en) * 1991-09-27 1994-01-04 Basf Aktiengesellschaft Flameproofed chlorine-and bromine-free molding composition
US5276077A (en) * 1992-06-03 1994-01-04 The Dow Chemical Company Ignition resistant carbonate polymer blends
US5364899A (en) * 1992-01-24 1994-11-15 Denki Kagaku Koguo Kabushiki Kaisha Flame-retardant resin composition
EP0693495A1 (en) 1994-07-22 1996-01-24 Bayer Ag Phosphoric acid esters having several phosphor atoms
EP0714932A2 (en) * 1994-12-01 1996-06-05 Cheil Industries Inc. Flame proof polycarbonate composition
EP0716125A2 (en) 1994-12-05 1996-06-12 Bayer Ag Flame retardant thermoplastic polycarbonate moulding compositions
EP0761746A1 (en) 1995-08-17 1997-03-12 Bayer Ag Ultrafine inorganic powders as flame retardants in thermoplastic moulding compositions
AU676590B2 (en) * 1993-09-08 1997-03-13 Teijin Chemicals Ltd Resin composition and molded article
US5627228A (en) * 1994-05-10 1997-05-06 Daicel Chemical Industries, Ltd. Flame-retardant resin composition
US5658974A (en) * 1994-10-14 1997-08-19 Bayer Ag Flameproofed, thermoplastic polycarbonate moulding compounds
US5672645A (en) * 1993-08-26 1997-09-30 Bayer Ag Flame resistant polycarbonate/ABS moulding compounds resistant to stress cracking
US5674924A (en) * 1995-08-19 1997-10-07 Cheil Industries Inc. Flameproof thermoplastic resin compositions
US5723526A (en) * 1993-09-08 1998-03-03 Teijin Chemicals Ltd Resin composition and molded article
US5750602A (en) * 1995-10-19 1998-05-12 Bayer Ag Flameproofed polycarbonate/ABS blends resistant to stress cracking
EP0953604A2 (en) * 1998-04-27 1999-11-03 Techno Polymer Co., Ltd. Thermoplastic resin composition
US6043310A (en) * 1994-05-31 2000-03-28 General Electric Company Thin-wall housing
US6071992A (en) * 1997-07-23 2000-06-06 Techno Polymer Co., Ltd. Flame-retardant thermoplastic resin composition
US6083428A (en) * 1995-03-07 2000-07-04 Asahi Kasei Kogyo Kabushiki Kaisha Flame-retardant resin composition
US6096821A (en) * 1999-04-02 2000-08-01 General Electric Company Polyphenylene ether resin concentrates
US6117542A (en) * 1997-02-17 2000-09-12 Asahi Kasei Kogyo Kabushiki Kaisha Flame retardant resin composition
US6127465A (en) * 1997-09-04 2000-10-03 Idemitsu Petrochemical Co., Ltd. Polycarbonate resin composition
KR100278144B1 (en) * 1998-07-22 2001-01-15 유현식 Thermoplastic resin composition
US6174945B1 (en) 1999-06-14 2001-01-16 Lg Chemical Ltd. Halogen-free flameproof thermoplastic molding materials
US6228149B1 (en) 1999-01-20 2001-05-08 Patterson Technique, Inc. Method and apparatus for moving, filtering and ionizing air
US6258879B1 (en) 1999-04-02 2001-07-10 General Electric Company Polyphenylene ether resin concentrates containing organic phosphates
US6316579B1 (en) 1997-07-23 2001-11-13 Daicel Chemical Industries, Ltd. Polycarbonate resin composition containing block copolymer
US6319432B1 (en) 1999-06-11 2001-11-20 Albemarle Corporation Bisphenol-A bis(diphenyl phosphate)-based flame retardant
US6331584B1 (en) * 1998-09-29 2001-12-18 Idemitsu Petrochemical Co., Ltd. Flame-retardant polycarbonate resin composition and its injection moldings
US6342550B1 (en) 1999-02-03 2002-01-29 Mitsubishi Engineering Plastics Corporation Flame-retardent polycarbonate resin composition and a molded product using the same
US6359043B1 (en) 1998-09-24 2002-03-19 General Electric Company Mica as flame retardant in glass filled noryl
US6399685B1 (en) 2000-12-11 2002-06-04 Albemarle Corporation Purification of arylene polyphosphate esters
US6403683B1 (en) 1998-08-28 2002-06-11 Teijin Chemicals Ltd Polycarbonate resin composition and molded article
WO2002046305A1 (en) * 2000-12-08 2002-06-13 Bayer Aktiengesellschaft Polycarbonate compositions
US6417256B1 (en) * 1997-09-29 2002-07-09 Bayer Aktiengesellschaft Polycarbonate-ABS moulding materials
US6437029B1 (en) 2000-10-31 2002-08-20 Cheil Industries Inc. Flame retardant polycarbonate resin composition
US6448316B1 (en) 1997-09-18 2002-09-10 Mitsubishi Engineering-Plastics Corporation Flame retardant polycarbonate-styrene (or acrylate) polymers, and/or copolymers and/or graft polymer/copolymer mixtures
US20020137821A1 (en) * 2001-01-09 2002-09-26 Andreas Seidel Flame retardants which contain phosphorus, and flame-retardant thermoplastic molding compositions
KR100327501B1 (en) * 1998-07-14 2002-10-11 제일모직주식회사 Flame retardant thermoplastic resin conposition
US6503628B1 (en) * 1998-06-17 2003-01-07 Bayer Corporation Thermoplastic polycarbonate molding composition containing a rubber free copolymer and a combination of graft polymers
US6528561B1 (en) 1999-09-02 2003-03-04 Bayer Aktiengesellschaft Flame-resistant polycarbonate ABS blends
KR100375820B1 (en) * 2000-12-07 2003-03-15 제일모직주식회사 Flame Retardant Thermoplastic Resin Composition
US20030092805A1 (en) * 2000-03-06 2003-05-15 Andreas Seidel Flame-resistant polycarbonate moulding compounds for extrusion applications
US6569930B1 (en) 1997-08-11 2003-05-27 Bayer Aktiengesellschaft Flame and stress crack resistant polycarbonate molding compositions
US20030105196A1 (en) * 2000-03-06 2003-06-05 Andreas Seidel Flame-resistant polycarbonate moulding compounds
US6583204B1 (en) 1998-11-18 2003-06-24 Bayer Aktiengesellschaft Flame resistant thermostable polycarbonate ABS moulding compounds
US6593404B1 (en) 1997-10-23 2003-07-15 Cheil Industries, Inc. Thermoplastic resin composition
US20030158304A1 (en) * 2000-06-02 2003-08-21 Torsten Derr Non-inflammable, translucent polycarbonate molding materials
US20030171472A1 (en) * 2000-06-02 2003-09-11 Andreas Seidel Non-inflammable, anti-electrostatic polycarbonate molding materials
US6706788B2 (en) * 1997-05-23 2004-03-16 Bayer Aktiengesellschaft Flame-resistant polycarbonate moulding materials which are dimensionally stable at high temperatures and have high flow line strength
US20040059031A1 (en) * 2002-07-29 2004-03-25 Andreas Seidel Flame-resistant polycarbonate molding compositions
US6713544B2 (en) 2000-12-08 2004-03-30 Bayer Aktiengesellschaft Flame-resistant and heat-resistant polycarbonate compositions
US20040063824A1 (en) * 2001-11-22 2004-04-01 Makoto Takagi Flame-retardant resin composition
US6740696B1 (en) * 1995-11-01 2004-05-25 General Electric Company Flame retardant polycarbonate/graft copolymer blends exhibiting heat aging stability
US20040110879A1 (en) * 2002-12-06 2004-06-10 Andreas Seidel Flame-resistant polycarbonate compositions containing phosphorus-silicon compounds
US6753364B1 (en) 1999-09-02 2004-06-22 Bayer Aktiengesellschaft Flame-resistant polycarbonate molding materials
US6756433B1 (en) 1999-09-02 2004-06-29 Bayer Aktiengesellschaft Flame-resistant polycarbonate ABS moulding materials
US6784232B1 (en) 1999-09-02 2004-08-31 Bayer Aktiengesellschaft Flame-resistant polycarbonate blends
WO2004076546A1 (en) * 2003-02-24 2004-09-10 Dow Global Technologies Inc. Ignition resistant polymer compositions
US6815476B1 (en) 1995-06-07 2004-11-09 General Electric Company Phosphate flame retardant polymers
US20040235999A1 (en) * 2001-09-21 2004-11-25 Marc Vathauer Modified shock-resistant polymer compositions
US20040249070A1 (en) * 2001-09-03 2004-12-09 Lim Jong Cheol Flame retardant thermoplastic resin composition
US20040249027A1 (en) * 2001-09-13 2004-12-09 Cheil Industries Inc. Flame retardant thermoplastic resin composition
US6831120B1 (en) 1999-09-02 2004-12-14 Bayer Aktiengesellschaft Flame-resistant polycarbonate blends
KR100456484B1 (en) * 1998-12-24 2005-04-06 제일모직주식회사 Flameproof polycarbonate-based thermoplastic resin composition
KR100485652B1 (en) * 2001-10-11 2005-04-27 제일모직주식회사 Flame Retardant Thermoplastic Resin Composition
US6906122B1 (en) 1999-09-02 2005-06-14 Bayer Aktiengesellschaft Flame-resistant polycarbonate blends
US6914089B2 (en) 2000-12-08 2005-07-05 Bayer Aktiengesellschaft Flame-resistant polycarbonate blends
US6936647B2 (en) 2000-03-09 2005-08-30 Bayer Aktiengesellschaft Bead polymerizates containing halogen-free phosphourus compounds
US20050245648A1 (en) * 2002-07-11 2005-11-03 Cheil Industries Inc Flame retardant thermoplastic resin composition
US20060014863A1 (en) * 2002-07-08 2006-01-19 Cheil Industries Inc Flame retardant thermoplastic resin composition
KR100574085B1 (en) * 2000-05-29 2006-04-27 제일모직주식회사 Flame Retardant Thermoplastic Resin Composition
US20070060678A1 (en) * 2005-09-14 2007-03-15 Eckhard Wenz Thermoplastic molding composition and articles thermoformed therefrom
US20070082995A1 (en) * 2003-11-07 2007-04-12 Italmatch Chemicals S.P.A. Halogen-free flame retardant polycarbonate compositions
US20070155873A1 (en) * 2005-12-30 2007-07-05 Kang Tae G Flame retardant polycarbonate thermoplastic resin composition having good extrusion moldability and impact resistance
US20070232730A1 (en) * 2004-09-09 2007-10-04 Shin-Etsu Chemical Co., Ltd. Polyphenylene ether oligomer sulfonic acid salt, making method, flame retardant resin composition, and molded article
US20070244229A1 (en) * 2004-06-17 2007-10-18 Hong Sang H Flameproof Thermoplastic Resin Composition
US20070249768A1 (en) * 2004-12-30 2007-10-25 Cheil Industries Inc. Flame Retardant Polycarbonate Resin Composition
US20070249767A1 (en) * 2005-12-30 2007-10-25 Cheil Industries Inc. Flame Retardant Polycarbonate Thermoplastic Resin Composition Having Good Extrusion Moldability and Impact Resistance
US20070295946A1 (en) * 2004-10-13 2007-12-27 Cheil Industries Inc. Flame Retardant Thermoplastic Resin Composition
US20080108737A1 (en) * 2006-06-06 2008-05-08 Shin-Etsu Chemical Co., Ltd. Additive for imparting flame retardance with an organic resin, flame retardant resin composition, and article molded therefrom
US20080275161A1 (en) * 2004-06-18 2008-11-06 Sang Hyun Hong Flameproof Thermoplastic Resin Composition
US20090012217A1 (en) * 2007-07-02 2009-01-08 Cheil Industries Inc. Flameproof Thermoplastic Resin Composition
US20090118402A1 (en) * 2006-04-14 2009-05-07 Cheil Industries Inc. Scratch-Resistant Flameproof Thermoplastic Resin Composition
US20090149587A1 (en) * 2007-12-10 2009-06-11 Cheil Industries Inc. Sterically Hindered Phenolic Phosphonates and Polycarbonate Resin Composition Using the Same
WO2009094241A2 (en) * 2008-01-14 2009-07-30 Dow Global Technologies Inc. Ignition resistant carbonate polymer composition containing an aromatic phosphonate
US20090203819A1 (en) * 2006-11-23 2009-08-13 Cheil Industries Inc. Flameproof Thermoplastic Resin Composition
US20090290345A1 (en) * 2008-05-20 2009-11-26 Apl Ip Holding Llc Enclosures for led circuit boards
US20100152357A1 (en) * 2008-12-17 2010-06-17 Cheil Industries Inc. Polycarbonate Resin Composition with Improved Transparency and Scratch-Resistance
US20100168296A1 (en) * 2008-12-29 2010-07-01 Cheil Industries Inc. Flameproof Thermoplastic Resin Composition
US20100216922A1 (en) * 2007-11-19 2010-08-26 Cheil Industries Inc. Non-Halogen Flameproof Polycarbonate Resin Composition
US20100240831A1 (en) * 2007-12-18 2010-09-23 Cheil Industries Inc. Branched (Meth)acrylate Copolymer with High Refractive Index and Method for Preparing the Same
US20100256288A1 (en) * 2007-12-18 2010-10-07 Cheil Industries Inc. Scratch-Resistant Flameproof Thermoplastic Resin Composition with Improved Compatibility
US20110021677A1 (en) * 2008-04-14 2011-01-27 Cheil Industries Inc. Flame-Retardant Scratch-Resistant Thermoplastic Resin Composition with Improved Compatibility
US20110040019A1 (en) * 2008-03-13 2011-02-17 Cheil Industries Inc. Thermoplastic resin composition with improved compatibility
US20110065848A1 (en) * 2008-05-14 2011-03-17 Cheil Industries Inc. Flame Retardant Polycarbonate Resin Composition
US20110144239A1 (en) * 2009-12-11 2011-06-16 Cheil Industries Inc. Glass Fiber-Reinforced Polyester Resin Composition and Molded Product Using the Same
EP2336232A1 (en) 2009-12-21 2011-06-22 Cheil Industries Inc. Non-halogen flameproof polycarbonate resin composition
CN102108200A (en) * 2009-12-29 2011-06-29 第一毛织株式会社 Flame retardant polycarbonate resin composition
US20110160377A1 (en) * 2009-12-30 2011-06-30 Cheil Industries Inc. Thermoplastic Resin Composition Having Improved Impact Strength and Melt Flow Properties
US20110160367A1 (en) * 2009-12-31 2011-06-30 Cheil Industries Inc. Polycarbonate Resin Composition Having Good Flame Retardancy
WO2011107273A1 (en) 2010-03-02 2011-09-09 Styron Europe Gmbh Improved flow ignition resistant carbonate polymer composition
WO2011110365A1 (en) 2010-03-11 2011-09-15 Styron Europe Gmbh Impact modified ignition resistant carbonate polymer composition
CN101469115B (en) * 2007-12-25 2012-02-29 上海普利特复合材料股份有限公司 High flowability and high tenacity polycarbonate composition
US9006333B2 (en) 2010-09-30 2015-04-14 Daikin Industries, Ltd. Method for manufacturing fine polytetrafluoroethylene powder
TWI492984B (en) * 2007-08-17 2015-07-21 Mitsubishi Chemical Europe Gmbh Aromatic polycarbonate composition
US9309335B2 (en) 2010-09-30 2016-04-12 Daikin Industries, Ltd. Process for producing polytetrafluoroethylene fine powder
US9365671B2 (en) 2013-12-04 2016-06-14 Samsung Sdi Co., Ltd. Styrene-based copolymer and thermoplastic resin composition including the same
US9458316B2 (en) 2010-09-30 2016-10-04 Daikin Industries, Ltd. Dripping inhibitor and resin compound
US9732214B2 (en) 2011-12-22 2017-08-15 Lotte Advanced Materials Co., Ltd. Thermoplastic resin composition and molding form for same
US9790362B2 (en) 2014-06-27 2017-10-17 Lotte Advanced Materials Co., Ltd. Thermoplastic resin composition and molded article made using the same
US9850333B2 (en) 2014-06-27 2017-12-26 Lotte Advanced Materials Co., Ltd. Copolymers and thermoplastic resin composition including the same
US9856371B2 (en) 2014-06-27 2018-01-02 Lotte Advanced Materials Co., Ltd. Thermoplastic resin composition and low-gloss molded article made therefrom
US9862822B2 (en) 2014-11-18 2018-01-09 Lotte Advanced Materials Co., Ltd. Thermoplastic resin composition and molded article made using the same
US9902850B2 (en) 2014-06-26 2018-02-27 Lotte Advanced Materials Co., Ltd. Thermoplastic resin composition
US10640624B2 (en) 2016-12-22 2020-05-05 Lotte Advanced Materials Co., Ltd. Thermoplastic resin composition and article using the same
CN111117182A (en) * 2018-10-31 2020-05-08 乐天尖端材料株式会社 Thermoplastic resin composition and molded article formed therefrom
WO2020111618A1 (en) 2018-11-26 2020-06-04 롯데케미칼 주식회사 Thermoplastic resin composition and article produced therefrom
WO2020138802A1 (en) 2018-12-28 2020-07-02 롯데케미칼 주식회사 Thermoplastic resin composition and molded article therefrom

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5036126A (en) * 1990-05-30 1991-07-30 General Electric Company Flame retardant blends of polycarbonate, ABS and a terpolymer
DE4024670A1 (en) * 1990-08-03 1992-02-06 Bayer Ag Fire retardant mixts. for polycarbonate(s) - comprise boron phosphate, aromatic alkali sulphonate and tetra:fluoroethylene polymer
DE4024667C2 (en) * 1990-08-03 1997-04-30 Bayer Ag Flame retardants for polycarbonates and process for incorporation in polycarbonates
DE4033806A1 (en) * 1990-10-24 1992-04-30 Bayer Ag LIGHT AGING RESISTANT POLYCARBONATE MOLDS
EP0483510A3 (en) * 1990-10-31 1992-09-02 General Electric Company Polycarbonate compositions with improved appearance and flammability characteristics
DE19523086A1 (en) * 1995-06-26 1997-01-02 Bayer Ag Use of polymer molding compounds for partial color changes by laser energy to generate optical information with very good contrasts
SG72704A1 (en) * 1995-11-01 2000-05-23 Gen Electric Flame retardant thermoplastic composition containing aromatic polycarbonate resins and a rubber modified graft copolymer
DE19544675A1 (en) 1995-11-30 1997-06-05 Bayer Ag Polymer molding compounds stabilized with phosphorous acid esters
DE19620993A1 (en) * 1996-05-24 1997-11-27 Bayer Ag Laser-inscribable polymer molding compounds
JP4609978B2 (en) 1999-07-19 2011-01-12 三菱鉛筆株式会社 Writing instrument
JP2003003060A (en) * 2001-06-25 2003-01-08 Mitsubishi Engineering Plastics Corp Polycarbonate resin composition, method for producing the same and molding using the same
JP3891272B2 (en) 2002-03-05 2007-03-14 信越化学工業株式会社 Flame retardant resin composition and molded product thereof
DE102009020544A1 (en) 2009-05-08 2010-11-11 Heinrich-Heine-Universität Düsseldorf Preparing a copolymer, useful to produce e.g. plastics, comprises providing a cyclodextrin compound, providing a metallocene compound with double bonds and providing a styrene compound, adding an initiator and polymerizing components
MX2016004931A (en) * 2013-10-18 2016-12-20 Covestro Deutschland Ag Polycarbonate compositions having improved adhesion to polyurethane layers.
WO2023145342A1 (en) 2022-01-28 2023-08-03 帝人株式会社 Flame retardant polycarbonate resin composition and molded article thereof

Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4381359A (en) * 1979-07-19 1983-04-26 Bayer Aktiengesellschaft Stabilized thermoplastic moulding compositions
DE3430234A1 (en) * 1984-08-17 1986-02-27 Bayer Ag, 5090 Leverkusen FLAME-RESISTANT, THERMOPLASTIC POLYMER BLENDS
EP0174493A1 (en) * 1984-08-17 1986-03-19 Bayer Ag Thermoplastic moulding masses with flame-retarding properties
EP0207359A2 (en) * 1985-06-29 1987-01-07 Bayer Ag Thermoplastic moulding compositions having flame-retardant properties
US4649168A (en) * 1984-11-20 1987-03-10 Bayer Aktiengesellschaft Process for the preparation of flame-resistant polycarbonate moulding compositions containing tetrafluoroethylene polymers
DE3545609A1 (en) * 1985-12-21 1987-06-25 Bayer Ag METHOD FOR PRODUCING THERMOPLASTIC MOLDING MATERIALS WITH FLAME-RESISTANT PROPERTIES
US4692488A (en) * 1985-06-29 1987-09-08 Bayer Aktiengesellschaft Thermoplastic polycarbonate moulding compositions
EP0248308A2 (en) * 1986-06-06 1987-12-09 Bayer Ag Moulding compounds with easy mould releasability
DE3629546A1 (en) * 1986-08-30 1988-03-03 Bayer Ag IMPACT TOE, FLAME-RESISTANT MOLDS
DE3628904A1 (en) * 1986-08-26 1988-03-03 Bayer Ag IMPACT TOE, FLAME-RESISTANT POLYCARBONATE MOLDINGS
US4766165A (en) * 1985-06-14 1988-08-23 Bayer Aktiengesellschaft Thermoplastic moulding compositions having flame-retarding properties
CA1248661A (en) * 1983-06-21 1989-01-10 Christian Lindner Moulding compositions having flame-resistant properties
US4880875A (en) * 1986-05-09 1989-11-14 Basf Aktiengesellschaft Thermoplastic molding material based on polycarbonate, ASA and vinylaromatics/an-containing copolymers
US4914144A (en) * 1987-12-17 1990-04-03 Basf Aktiengesellschaft Halogen-free flameproof molding materials

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS518234A (en) * 1974-07-15 1976-01-23 Gen Electric HOKOZOKUEETERUMUSUIBUTSUNO SEIHO
AU8671075A (en) * 1974-12-06 1977-05-26 Gen Electric Flame retardant, non-dripping composition of polyphenylene ether and acrylonitrile - butadiene-styrene
DE3544295A1 (en) * 1985-12-14 1987-06-19 Bayer Ag THERMOPLASTIC MOLDS WITH HIGH CROSS-CURRENT RESISTANCE
JPS6391852A (en) * 1986-10-07 1988-04-22 Toshiba Corp Information recording method
JPS6391851A (en) * 1986-10-07 1988-04-22 Toshiba Corp Information recorder
JPS63110257A (en) * 1986-10-28 1988-05-14 Idemitsu Petrochem Co Ltd Flame retardant resin composition

Patent Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4381359A (en) * 1979-07-19 1983-04-26 Bayer Aktiengesellschaft Stabilized thermoplastic moulding compositions
CA1248661A (en) * 1983-06-21 1989-01-10 Christian Lindner Moulding compositions having flame-resistant properties
DE3430234A1 (en) * 1984-08-17 1986-02-27 Bayer Ag, 5090 Leverkusen FLAME-RESISTANT, THERMOPLASTIC POLYMER BLENDS
EP0174493A1 (en) * 1984-08-17 1986-03-19 Bayer Ag Thermoplastic moulding masses with flame-retarding properties
US4649168A (en) * 1984-11-20 1987-03-10 Bayer Aktiengesellschaft Process for the preparation of flame-resistant polycarbonate moulding compositions containing tetrafluoroethylene polymers
US4766165A (en) * 1985-06-14 1988-08-23 Bayer Aktiengesellschaft Thermoplastic moulding compositions having flame-retarding properties
EP0207359A2 (en) * 1985-06-29 1987-01-07 Bayer Ag Thermoplastic moulding compositions having flame-retardant properties
US4692488A (en) * 1985-06-29 1987-09-08 Bayer Aktiengesellschaft Thermoplastic polycarbonate moulding compositions
EP0226922A2 (en) * 1985-12-21 1987-07-01 Bayer Ag Process for preparing thermoplastic molding compositions with flame-retarding properties
DE3545609A1 (en) * 1985-12-21 1987-06-25 Bayer Ag METHOD FOR PRODUCING THERMOPLASTIC MOLDING MATERIALS WITH FLAME-RESISTANT PROPERTIES
US4880875A (en) * 1986-05-09 1989-11-14 Basf Aktiengesellschaft Thermoplastic molding material based on polycarbonate, ASA and vinylaromatics/an-containing copolymers
EP0248308A2 (en) * 1986-06-06 1987-12-09 Bayer Ag Moulding compounds with easy mould releasability
DE3628904A1 (en) * 1986-08-26 1988-03-03 Bayer Ag IMPACT TOE, FLAME-RESISTANT POLYCARBONATE MOLDINGS
DE3629546A1 (en) * 1986-08-30 1988-03-03 Bayer Ag IMPACT TOE, FLAME-RESISTANT MOLDS
US4914144A (en) * 1987-12-17 1990-04-03 Basf Aktiengesellschaft Halogen-free flameproof molding materials

Cited By (176)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5266618A (en) * 1991-05-28 1993-11-30 Denki Kagaku Kogyo Kabushiki Kaisha Flame-retardant resin composition
US5272193A (en) * 1991-07-12 1993-12-21 Bayer Aktiengesellschaft Thermoplastic polycarbonate moulding compounds with flame-resistant properties
US5219907A (en) * 1991-09-27 1993-06-15 Basf Aktiengesellschaft Flameproofed molding composition
US5276256A (en) * 1991-09-27 1994-01-04 Basf Aktiengesellschaft Flameproofed chlorine-and bromine-free molding composition
US5364899A (en) * 1992-01-24 1994-11-15 Denki Kagaku Koguo Kabushiki Kaisha Flame-retardant resin composition
US5276077A (en) * 1992-06-03 1994-01-04 The Dow Chemical Company Ignition resistant carbonate polymer blends
USRE36902E (en) * 1993-08-26 2000-10-03 Bayer Ag Flame resistant polycarbonate/abs moulding compounds resistant to stress cracking
US5672645A (en) * 1993-08-26 1997-09-30 Bayer Ag Flame resistant polycarbonate/ABS moulding compounds resistant to stress cracking
US5723526A (en) * 1993-09-08 1998-03-03 Teijin Chemicals Ltd Resin composition and molded article
AU676590B2 (en) * 1993-09-08 1997-03-13 Teijin Chemicals Ltd Resin composition and molded article
US6022917A (en) * 1994-05-10 2000-02-08 Daicel Chemical Industries, Ltd. Flame-retardant resin composition
US5994433A (en) * 1994-05-10 1999-11-30 Daicel Chemical Industries, Ltd. Flame-retardant resin composition
US5627228A (en) * 1994-05-10 1997-05-06 Daicel Chemical Industries, Ltd. Flame-retardant resin composition
US6043310A (en) * 1994-05-31 2000-03-28 General Electric Company Thin-wall housing
EP0685526B1 (en) * 1994-05-31 2001-08-29 General Electric Company Fire-resistant polycarbonate resin composition
EP0693495A1 (en) 1994-07-22 1996-01-24 Bayer Ag Phosphoric acid esters having several phosphor atoms
US5733957A (en) * 1994-07-22 1998-03-31 Bayer Ag Flame retardant polycarbonate containing polycyclic phosphoric acid esters
US5658974A (en) * 1994-10-14 1997-08-19 Bayer Ag Flameproofed, thermoplastic polycarbonate moulding compounds
EP0714932A3 (en) * 1994-12-01 1996-07-31 Cheil Ind Inc Flame proof polycarbonate composition
EP0714932A2 (en) * 1994-12-01 1996-06-05 Cheil Industries Inc. Flame proof polycarbonate composition
EP0716125A2 (en) 1994-12-05 1996-06-12 Bayer Ag Flame retardant thermoplastic polycarbonate moulding compositions
US5621029A (en) * 1994-12-05 1997-04-15 Bayer Ag Flame retardant thermoplastic polycarbonate moulding compositions
US6083428A (en) * 1995-03-07 2000-07-04 Asahi Kasei Kogyo Kabushiki Kaisha Flame-retardant resin composition
US6815476B1 (en) 1995-06-07 2004-11-09 General Electric Company Phosphate flame retardant polymers
EP0761746A1 (en) 1995-08-17 1997-03-12 Bayer Ag Ultrafine inorganic powders as flame retardants in thermoplastic moulding compositions
US5674924A (en) * 1995-08-19 1997-10-07 Cheil Industries Inc. Flameproof thermoplastic resin compositions
US5750602A (en) * 1995-10-19 1998-05-12 Bayer Ag Flameproofed polycarbonate/ABS blends resistant to stress cracking
US6740696B1 (en) * 1995-11-01 2004-05-25 General Electric Company Flame retardant polycarbonate/graft copolymer blends exhibiting heat aging stability
US6117542A (en) * 1997-02-17 2000-09-12 Asahi Kasei Kogyo Kabushiki Kaisha Flame retardant resin composition
DE19806573C5 (en) * 1997-02-17 2004-07-01 Asahi Kasei Kabushiki Kaisha Process for producing a flame retardant resin composition
US6706788B2 (en) * 1997-05-23 2004-03-16 Bayer Aktiengesellschaft Flame-resistant polycarbonate moulding materials which are dimensionally stable at high temperatures and have high flow line strength
US6316579B1 (en) 1997-07-23 2001-11-13 Daicel Chemical Industries, Ltd. Polycarbonate resin composition containing block copolymer
US6071992A (en) * 1997-07-23 2000-06-06 Techno Polymer Co., Ltd. Flame-retardant thermoplastic resin composition
US6569930B1 (en) 1997-08-11 2003-05-27 Bayer Aktiengesellschaft Flame and stress crack resistant polycarbonate molding compositions
US6127465A (en) * 1997-09-04 2000-10-03 Idemitsu Petrochemical Co., Ltd. Polycarbonate resin composition
US6448316B1 (en) 1997-09-18 2002-09-10 Mitsubishi Engineering-Plastics Corporation Flame retardant polycarbonate-styrene (or acrylate) polymers, and/or copolymers and/or graft polymer/copolymer mixtures
US6417256B1 (en) * 1997-09-29 2002-07-09 Bayer Aktiengesellschaft Polycarbonate-ABS moulding materials
US6593404B1 (en) 1997-10-23 2003-07-15 Cheil Industries, Inc. Thermoplastic resin composition
EP0953604A3 (en) * 1998-04-27 2001-04-11 Techno Polymer Co., Ltd. Thermoplastic resin composition
EP0953604A2 (en) * 1998-04-27 1999-11-03 Techno Polymer Co., Ltd. Thermoplastic resin composition
US6503628B1 (en) * 1998-06-17 2003-01-07 Bayer Corporation Thermoplastic polycarbonate molding composition containing a rubber free copolymer and a combination of graft polymers
KR100327501B1 (en) * 1998-07-14 2002-10-11 제일모직주식회사 Flame retardant thermoplastic resin conposition
KR100278144B1 (en) * 1998-07-22 2001-01-15 유현식 Thermoplastic resin composition
US6403683B1 (en) 1998-08-28 2002-06-11 Teijin Chemicals Ltd Polycarbonate resin composition and molded article
US6664362B2 (en) 1998-08-28 2003-12-16 Teijin Chemicals Ltd Polycarbonate resin composition and molded article
US6359043B1 (en) 1998-09-24 2002-03-19 General Electric Company Mica as flame retardant in glass filled noryl
US6331584B1 (en) * 1998-09-29 2001-12-18 Idemitsu Petrochemical Co., Ltd. Flame-retardant polycarbonate resin composition and its injection moldings
US6583204B1 (en) 1998-11-18 2003-06-24 Bayer Aktiengesellschaft Flame resistant thermostable polycarbonate ABS moulding compounds
KR100456484B1 (en) * 1998-12-24 2005-04-06 제일모직주식회사 Flameproof polycarbonate-based thermoplastic resin composition
US6228149B1 (en) 1999-01-20 2001-05-08 Patterson Technique, Inc. Method and apparatus for moving, filtering and ionizing air
US6342550B1 (en) 1999-02-03 2002-01-29 Mitsubishi Engineering Plastics Corporation Flame-retardent polycarbonate resin composition and a molded product using the same
US6096821A (en) * 1999-04-02 2000-08-01 General Electric Company Polyphenylene ether resin concentrates
US6486244B2 (en) 1999-04-02 2002-11-26 General Electric Company Polyphenylene ether resin concentrates containing organic phosphates
US6258879B1 (en) 1999-04-02 2001-07-10 General Electric Company Polyphenylene ether resin concentrates containing organic phosphates
US6319432B1 (en) 1999-06-11 2001-11-20 Albemarle Corporation Bisphenol-A bis(diphenyl phosphate)-based flame retardant
US6174945B1 (en) 1999-06-14 2001-01-16 Lg Chemical Ltd. Halogen-free flameproof thermoplastic molding materials
US6831120B1 (en) 1999-09-02 2004-12-14 Bayer Aktiengesellschaft Flame-resistant polycarbonate blends
US6528561B1 (en) 1999-09-02 2003-03-04 Bayer Aktiengesellschaft Flame-resistant polycarbonate ABS blends
US6784232B1 (en) 1999-09-02 2004-08-31 Bayer Aktiengesellschaft Flame-resistant polycarbonate blends
US6756433B1 (en) 1999-09-02 2004-06-29 Bayer Aktiengesellschaft Flame-resistant polycarbonate ABS moulding materials
US6753364B1 (en) 1999-09-02 2004-06-22 Bayer Aktiengesellschaft Flame-resistant polycarbonate molding materials
US6906122B1 (en) 1999-09-02 2005-06-14 Bayer Aktiengesellschaft Flame-resistant polycarbonate blends
US6939905B2 (en) 2000-03-06 2005-09-06 Bayer Aktiengesellschaft Flame-resistant polycarbonate molding compounds for extrusion applications
US6828366B2 (en) 2000-03-06 2004-12-07 Bayer Aktiengesellschaft Flame-resistant polycarbonate moulding compounds
CN101117434B (en) * 2000-03-06 2012-09-05 拜尔公司 Flame-resistant polycarbonate moulding compounds
US20030105196A1 (en) * 2000-03-06 2003-06-05 Andreas Seidel Flame-resistant polycarbonate moulding compounds
US20030092805A1 (en) * 2000-03-06 2003-05-15 Andreas Seidel Flame-resistant polycarbonate moulding compounds for extrusion applications
US6936647B2 (en) 2000-03-09 2005-08-30 Bayer Aktiengesellschaft Bead polymerizates containing halogen-free phosphourus compounds
KR100574085B1 (en) * 2000-05-29 2006-04-27 제일모직주식회사 Flame Retardant Thermoplastic Resin Composition
US6949596B2 (en) 2000-06-02 2005-09-27 Bayer Aktiengesellschaft Non-inflammable, anti-electrostatic polycarbonate molding materials
US6906124B2 (en) * 2000-06-02 2005-06-14 Bayer Aktiengesellschaft Non-inflammable, translucent polycarbonate molding materials
US20030171472A1 (en) * 2000-06-02 2003-09-11 Andreas Seidel Non-inflammable, anti-electrostatic polycarbonate molding materials
US20030158304A1 (en) * 2000-06-02 2003-08-21 Torsten Derr Non-inflammable, translucent polycarbonate molding materials
US6437029B1 (en) 2000-10-31 2002-08-20 Cheil Industries Inc. Flame retardant polycarbonate resin composition
KR100372569B1 (en) * 2000-10-31 2003-02-19 제일모직주식회사 Flame Retardant Thermoplastic Resin Composition
KR100375820B1 (en) * 2000-12-07 2003-03-15 제일모직주식회사 Flame Retardant Thermoplastic Resin Composition
US6713544B2 (en) 2000-12-08 2004-03-30 Bayer Aktiengesellschaft Flame-resistant and heat-resistant polycarbonate compositions
WO2002046305A1 (en) * 2000-12-08 2002-06-13 Bayer Aktiengesellschaft Polycarbonate compositions
US6914089B2 (en) 2000-12-08 2005-07-05 Bayer Aktiengesellschaft Flame-resistant polycarbonate blends
US6399685B1 (en) 2000-12-11 2002-06-04 Albemarle Corporation Purification of arylene polyphosphate esters
US7019056B2 (en) 2001-01-09 2006-03-28 Bayer Aktiengesellschaft Flame retardants which contain phosphorus, and flame-retardant thermoplastic molding compositions
US20020137821A1 (en) * 2001-01-09 2002-09-26 Andreas Seidel Flame retardants which contain phosphorus, and flame-retardant thermoplastic molding compositions
US20040249070A1 (en) * 2001-09-03 2004-12-09 Lim Jong Cheol Flame retardant thermoplastic resin composition
US7094818B2 (en) 2001-09-03 2006-08-22 Cheil Industries, Inc. Thermoplastic resin compositions containing mixtures of cyclic phosphazenes and phosphoric acid esters
US7550523B2 (en) 2001-09-13 2009-06-23 Cheil Industries Inc. Thermoplastic resin compositions containing mixtures of cyclic phosphazenes and phosphate ester morpholides
US20040249027A1 (en) * 2001-09-13 2004-12-09 Cheil Industries Inc. Flame retardant thermoplastic resin composition
US20040235999A1 (en) * 2001-09-21 2004-11-25 Marc Vathauer Modified shock-resistant polymer compositions
KR100485652B1 (en) * 2001-10-11 2005-04-27 제일모직주식회사 Flame Retardant Thermoplastic Resin Composition
US20040063824A1 (en) * 2001-11-22 2004-04-01 Makoto Takagi Flame-retardant resin composition
US6956073B2 (en) 2001-11-22 2005-10-18 Teijin Chemicals, Ltd. Flame-retardant resin composition
US20060014863A1 (en) * 2002-07-08 2006-01-19 Cheil Industries Inc Flame retardant thermoplastic resin composition
US7498370B2 (en) 2002-07-08 2009-03-03 Cheil Industries Inc. Flame retardant thermoplastic resin composition
US20050245648A1 (en) * 2002-07-11 2005-11-03 Cheil Industries Inc Flame retardant thermoplastic resin composition
US7511088B2 (en) 2002-07-11 2009-03-31 Cheil Industries Inc. Flame retardant thermoplastic resin composition
US20040059031A1 (en) * 2002-07-29 2004-03-25 Andreas Seidel Flame-resistant polycarbonate molding compositions
US7220790B2 (en) 2002-07-29 2007-05-22 Bayer Aktiengesellschaft Flame-resistant polycarbonate molding compositions
US20040110879A1 (en) * 2002-12-06 2004-06-10 Andreas Seidel Flame-resistant polycarbonate compositions containing phosphorus-silicon compounds
US7144935B2 (en) 2002-12-06 2006-12-05 Bayer Aktiengesellschaft Flame-resistant polycarbonate compositions containing phosphorus-silicon compounds
WO2004076546A1 (en) * 2003-02-24 2004-09-10 Dow Global Technologies Inc. Ignition resistant polymer compositions
US20070082995A1 (en) * 2003-11-07 2007-04-12 Italmatch Chemicals S.P.A. Halogen-free flame retardant polycarbonate compositions
US7608654B2 (en) * 2003-11-07 2009-10-27 Italamatch Chemicals S.P.A. Halogen-free flame retardant polycarbonate compositions
US20070244229A1 (en) * 2004-06-17 2007-10-18 Hong Sang H Flameproof Thermoplastic Resin Composition
US20080275161A1 (en) * 2004-06-18 2008-11-06 Sang Hyun Hong Flameproof Thermoplastic Resin Composition
US20070232730A1 (en) * 2004-09-09 2007-10-04 Shin-Etsu Chemical Co., Ltd. Polyphenylene ether oligomer sulfonic acid salt, making method, flame retardant resin composition, and molded article
US7511089B2 (en) 2004-09-09 2009-03-31 Shin-Etsu Chemical Co., Ltd. Polyphenylene ether oligomer sulfonic acid salt, making method, flame retardant resin composition, and molded article
US20070295946A1 (en) * 2004-10-13 2007-12-27 Cheil Industries Inc. Flame Retardant Thermoplastic Resin Composition
US8119726B2 (en) 2004-10-13 2012-02-21 Cheil Industries Inc. Flame retardant thermoplastic resin composition
US20070249768A1 (en) * 2004-12-30 2007-10-25 Cheil Industries Inc. Flame Retardant Polycarbonate Resin Composition
US7569629B2 (en) 2004-12-30 2009-08-04 Cheil Industries Inc. Flame retardant polycarbonate resin composition
US7446144B2 (en) 2005-09-14 2008-11-04 Bayer Materialscience Llc Thermoplastic molding composition and articles thermoformed therefrom
US20070060678A1 (en) * 2005-09-14 2007-03-15 Eckhard Wenz Thermoplastic molding composition and articles thermoformed therefrom
US20070249767A1 (en) * 2005-12-30 2007-10-25 Cheil Industries Inc. Flame Retardant Polycarbonate Thermoplastic Resin Composition Having Good Extrusion Moldability and Impact Resistance
US20070155873A1 (en) * 2005-12-30 2007-07-05 Kang Tae G Flame retardant polycarbonate thermoplastic resin composition having good extrusion moldability and impact resistance
US7659332B2 (en) 2005-12-30 2010-02-09 Cheil Industries Inc. Flame retardant polycarbonate thermoplastic resin composition having good extrusion moldability and impact resistance
US20090118402A1 (en) * 2006-04-14 2009-05-07 Cheil Industries Inc. Scratch-Resistant Flameproof Thermoplastic Resin Composition
US7732515B2 (en) 2006-04-14 2010-06-08 Cheil Industries Inc. Scratch-resistant flameproof thermoplastic resin composition
US7511091B2 (en) 2006-06-06 2009-03-31 Shin-Etsu Chemical Co., Ltd. Additive for imparting flame retardance with an organic resin, flame retardant resin composition, and article molded therefrom
US20080108737A1 (en) * 2006-06-06 2008-05-08 Shin-Etsu Chemical Co., Ltd. Additive for imparting flame retardance with an organic resin, flame retardant resin composition, and article molded therefrom
US20090203819A1 (en) * 2006-11-23 2009-08-13 Cheil Industries Inc. Flameproof Thermoplastic Resin Composition
US7786196B2 (en) 2006-11-23 2010-08-31 Cheil Industries Inc. Flameproof thermoplastic resin composition
US8492463B2 (en) 2007-07-02 2013-07-23 Cheil Industries Inc. Flameproof thermoplastic resin composition
US20090012217A1 (en) * 2007-07-02 2009-01-08 Cheil Industries Inc. Flameproof Thermoplastic Resin Composition
TWI492984B (en) * 2007-08-17 2015-07-21 Mitsubishi Chemical Europe Gmbh Aromatic polycarbonate composition
US8030380B2 (en) 2007-11-19 2011-10-04 Cheil Industries Inc. Non-halogen flameproof polycarbonate resin composition
US20100216922A1 (en) * 2007-11-19 2010-08-26 Cheil Industries Inc. Non-Halogen Flameproof Polycarbonate Resin Composition
DE102008061429A1 (en) 2007-12-10 2009-06-18 Cheil Industries Inc. Sterically hindered phenolic phosphonates and flameproof polycarbonate resin composition using the same
US7919548B2 (en) 2007-12-10 2011-04-05 Cheil Industries Inc. Sterically hindered phenolic phosphonates and polycarbonate resin composition using the same
US20090149587A1 (en) * 2007-12-10 2009-06-11 Cheil Industries Inc. Sterically Hindered Phenolic Phosphonates and Polycarbonate Resin Composition Using the Same
US8901218B2 (en) 2007-12-18 2014-12-02 Cheil Industries Inc. Branched (meth)acrylate copolymer with high refractive index and method for preparing the same
US20100240831A1 (en) * 2007-12-18 2010-09-23 Cheil Industries Inc. Branched (Meth)acrylate Copolymer with High Refractive Index and Method for Preparing the Same
US20100256288A1 (en) * 2007-12-18 2010-10-07 Cheil Industries Inc. Scratch-Resistant Flameproof Thermoplastic Resin Composition with Improved Compatibility
US8642693B2 (en) 2007-12-18 2014-02-04 Cheil Industries Inc. Scratch-resistant flameproof thermoplastic resin composition with improved compatibility
CN101469115B (en) * 2007-12-25 2012-02-29 上海普利特复合材料股份有限公司 High flowability and high tenacity polycarbonate composition
WO2009094241A3 (en) * 2008-01-14 2009-10-29 Dow Global Technologies Inc. Ignition resistant carbonate polymer composition containing an aromatic phosphonate
WO2009094241A2 (en) * 2008-01-14 2009-07-30 Dow Global Technologies Inc. Ignition resistant carbonate polymer composition containing an aromatic phosphonate
US8658720B2 (en) 2008-03-13 2014-02-25 Cheil Industries Inc. Thermoplastic resin composition with improved compatibility
US20110040019A1 (en) * 2008-03-13 2011-02-17 Cheil Industries Inc. Thermoplastic resin composition with improved compatibility
US8772401B2 (en) 2008-04-14 2014-07-08 Cheil Industries Inc. Flame-retardant scratch-resistant thermoplastic resin composition with improved compatibility
US20110021677A1 (en) * 2008-04-14 2011-01-27 Cheil Industries Inc. Flame-Retardant Scratch-Resistant Thermoplastic Resin Composition with Improved Compatibility
US20110065848A1 (en) * 2008-05-14 2011-03-17 Cheil Industries Inc. Flame Retardant Polycarbonate Resin Composition
US20090290345A1 (en) * 2008-05-20 2009-11-26 Apl Ip Holding Llc Enclosures for led circuit boards
US7845829B2 (en) 2008-05-20 2010-12-07 Abl Ip Holding Llc Enclosures for LED circuit boards
US8940836B2 (en) 2008-12-17 2015-01-27 Cheil Industries Inc. Polycarbonate resin composition with improved transparency and scratch-resistance
US20100152357A1 (en) * 2008-12-17 2010-06-17 Cheil Industries Inc. Polycarbonate Resin Composition with Improved Transparency and Scratch-Resistance
US20100168296A1 (en) * 2008-12-29 2010-07-01 Cheil Industries Inc. Flameproof Thermoplastic Resin Composition
US8008382B2 (en) 2008-12-29 2011-08-30 Cheil Industries Inc. Flameproof thermoplastic resin composition
US20110144239A1 (en) * 2009-12-11 2011-06-16 Cheil Industries Inc. Glass Fiber-Reinforced Polyester Resin Composition and Molded Product Using the Same
US8546469B2 (en) 2009-12-11 2013-10-01 Cheil Industries Inc. Glass fiber-reinforced polyester resin composition and molded product using the same
US8133946B2 (en) 2009-12-21 2012-03-13 Cheil Industries Inc. Non-halogen flameproof polycarbonate resin composition
US20110152415A1 (en) * 2009-12-21 2011-06-23 Cheil Industries Inc. Non-Halogen Flameproof Polycarbonate Resin Composition
EP2336232A1 (en) 2009-12-21 2011-06-22 Cheil Industries Inc. Non-halogen flameproof polycarbonate resin composition
CN102108200A (en) * 2009-12-29 2011-06-29 第一毛织株式会社 Flame retardant polycarbonate resin composition
US20110160365A1 (en) * 2009-12-29 2011-06-30 Cheil Industries Inc. Flame Retardant Polycarbonate Resin Composition
US20110160377A1 (en) * 2009-12-30 2011-06-30 Cheil Industries Inc. Thermoplastic Resin Composition Having Improved Impact Strength and Melt Flow Properties
EP2341098A1 (en) 2009-12-31 2011-07-06 Cheil Industries Inc. Polycarbonate resin composition
US20110160367A1 (en) * 2009-12-31 2011-06-30 Cheil Industries Inc. Polycarbonate Resin Composition Having Good Flame Retardancy
US8222330B2 (en) 2009-12-31 2012-07-17 Cheil Industries Inc. Polycarbonate resin composition having good flame retardancy
WO2011107273A1 (en) 2010-03-02 2011-09-09 Styron Europe Gmbh Improved flow ignition resistant carbonate polymer composition
WO2011110365A1 (en) 2010-03-11 2011-09-15 Styron Europe Gmbh Impact modified ignition resistant carbonate polymer composition
US9006333B2 (en) 2010-09-30 2015-04-14 Daikin Industries, Ltd. Method for manufacturing fine polytetrafluoroethylene powder
US9309335B2 (en) 2010-09-30 2016-04-12 Daikin Industries, Ltd. Process for producing polytetrafluoroethylene fine powder
US9458316B2 (en) 2010-09-30 2016-10-04 Daikin Industries, Ltd. Dripping inhibitor and resin compound
US9475935B2 (en) 2010-09-30 2016-10-25 Daikin Industries, Ltd. Dripping inhibitor and resin compound
US9732214B2 (en) 2011-12-22 2017-08-15 Lotte Advanced Materials Co., Ltd. Thermoplastic resin composition and molding form for same
US9365671B2 (en) 2013-12-04 2016-06-14 Samsung Sdi Co., Ltd. Styrene-based copolymer and thermoplastic resin composition including the same
US9902850B2 (en) 2014-06-26 2018-02-27 Lotte Advanced Materials Co., Ltd. Thermoplastic resin composition
US9790362B2 (en) 2014-06-27 2017-10-17 Lotte Advanced Materials Co., Ltd. Thermoplastic resin composition and molded article made using the same
US9850333B2 (en) 2014-06-27 2017-12-26 Lotte Advanced Materials Co., Ltd. Copolymers and thermoplastic resin composition including the same
US9856371B2 (en) 2014-06-27 2018-01-02 Lotte Advanced Materials Co., Ltd. Thermoplastic resin composition and low-gloss molded article made therefrom
US9862822B2 (en) 2014-11-18 2018-01-09 Lotte Advanced Materials Co., Ltd. Thermoplastic resin composition and molded article made using the same
US10640624B2 (en) 2016-12-22 2020-05-05 Lotte Advanced Materials Co., Ltd. Thermoplastic resin composition and article using the same
CN111117182A (en) * 2018-10-31 2020-05-08 乐天尖端材料株式会社 Thermoplastic resin composition and molded article formed therefrom
CN111117182B (en) * 2018-10-31 2022-06-03 乐天尖端材料株式会社 Thermoplastic resin composition and molded article formed therefrom
US11492487B2 (en) 2018-10-31 2022-11-08 Lotte Advanced Materials Co., Ltd. Thermoplastic resin composition and article produced therefrom
WO2020111618A1 (en) 2018-11-26 2020-06-04 롯데케미칼 주식회사 Thermoplastic resin composition and article produced therefrom
WO2020138802A1 (en) 2018-12-28 2020-07-02 롯데케미칼 주식회사 Thermoplastic resin composition and molded article therefrom

Also Published As

Publication number Publication date
EP0345522A3 (en) 1990-12-05
JPH0670177B2 (en) 1994-09-07
DE58909840D1 (en) 1998-10-01
JPH0232154A (en) 1990-02-01
DE3819081A1 (en) 1989-12-07
ES2120943T3 (en) 1998-11-16
EP0345522B1 (en) 1998-08-26
EP0345522A2 (en) 1989-12-13

Similar Documents

Publication Publication Date Title
US5061745A (en) Flame-retardant, high-impact polycarbonate molding compounds
US4920166A (en) Flame-resistant, antistatic polycarbonate molding compositions
US4692488A (en) Thermoplastic polycarbonate moulding compositions
US4988748A (en) Flame-resistant thermoplastic polycarbonate molding compounds
US4751260A (en) Flame-retarding, polycarbonate moulding materials of high impact strength
US4983658A (en) Thermoplastic moulding compositions with flame-repellent properties
US5672645A (en) Flame resistant polycarbonate/ABS moulding compounds resistant to stress cracking
US4883835A (en) Flame resistant antistatic polycarbonate moulding compounds
US6590015B1 (en) Flame-resistant molding compounds
US4766165A (en) Thermoplastic moulding compositions having flame-retarding properties
US5030675A (en) Flame-resistant thermoplastic moulding compounds based on polycarbonate, polyalkylene terephthalate, graft copolymer, fluorinated polyolefine and phosphorus compound
US6569930B1 (en) Flame and stress crack resistant polycarbonate molding compositions
US5552465A (en) Polycarbonate molding compounds stable to light ageing
MXPA02002293A (en) Flameresistant polycarbonate abs blends.
US5741838A (en) Flame retardent thermoplastic polycarbonate moulding compounds
CA2290567C (en) Flame-resistant polycarbonate moulding materials which are dimensionally stable at high temperatures and have high flow line strength
US5137953A (en) Flame-resistant thermoplastic polycarbonate molding compounds
US4925891A (en) High impact strength flame-retardant polycarbonate moulding compositions
JPH064758B2 (en) Flame-retardant thermoplastic molding composition
JPS6368661A (en) High impact resistant-flame resistant molding composition
JPS62285948A (en) Thermoplastic molding compound
US5733957A (en) Flame retardant polycarbonate containing polycyclic phosphoric acid esters
JPH11315200A (en) Flame-retardant carbonate polymer composition having improved stability to hydrolysis
MXPA02002299A (en) Flameresistant polycarbonate blends.
EP0574054B1 (en) Flame retardant thermoplastic composition containing an impact-resistant vinyl aromatic copolymer

Legal Events

Date Code Title Description
AS Assignment

Owner name: BAYER AKTIENGESELLSCHAFT, LEVERKUSEN, GERMANY, A C

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNORS:WITTMANN, DIETER;PETERS, HORST;SCHOEPS, JOCHEN;AND OTHERS;REEL/FRAME:005085/0208;SIGNING DATES FROM 19890505 TO 19890515

STCF Information on status: patent grant

Free format text: PATENTED CASE

FEPP Fee payment procedure

Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

FPAY Fee payment

Year of fee payment: 4

FPAY Fee payment

Year of fee payment: 8

FPAY Fee payment

Year of fee payment: 12

SULP Surcharge for late payment

Year of fee payment: 11